危险废物焚烧飞灰中重金属的稳定化处理

以上海市某危险废物焚烧厂飞灰为研究对象,采用Na2S、FeSO4、Na3PO4、和Na3C3N3S34种不同类型化学稳定药剂对飞灰进行了稳定化处理,并应用XRD、IR、SEM和连续化学提取法等仪器和手段对Na3C3N3S3处理焚烧飞灰的产物进行分析研究。研究结果表明,Na3C3N3S3对飞灰中的重金属Cr、Pb、Zn的稳定效果最好,Na3PO4对Cr无明显稳定效果。稳定后产物表面变得致密化,Na3C3N3S3与重金属离子生成的沉淀物干燥后无明显晶型存在。经稳定处理后飞灰中的重金属形态由弱酸提取态转化为可氧化态,减少了飞灰中重金属的浸出毒性。     

有机磷酸HEDP稳定垃圾焚烧飞灰重金属的研究

研究了有机磷酸羟基亚乙基二膦酸（HEDP）对生活垃圾焚烧飞灰中重金属的稳定方法.通过对不同HEDP投加量处理后的飞灰试样作危险废物浸出毒性鉴别试验,分析HEDP最佳使用剂量,并评价了稳定化飞灰的长期稳定性.结果表明,HEDP最适使用剂量为0.03 Ml/g（以商品级HEDP与飞灰的体积质量比计）,处理后飞灰与原状飞灰相比,Pb、Zn和Hg的浸出浓度分别降低了98.3%、99.5%和85.0%.HEDP对飞灰中重金属稳定效果排序为：Pb＞Zn＞Hg＞Ni＞Cu＞Cd＞CrHAs.重金属pH相关浸出测试（pH-dependent leaching tests）表明：经0.03mL/g HEDP稳定处理的飞灰,在0.3 mol/L HNO3和0.3 mol/L NaOH的浸取条件下,其重金属浸出浓度均低于国家危险废物鉴别标准,显示具有良好的长期稳定性.     

满足《生活垃圾填埋污染控制标准》的生活垃圾焚烧飞灰重金属药剂稳定化研究

基于<生活垃圾填埋污染控制标准>(GB 16889-2008)对生活垃圾焚烧飞灰(以下简称飞灰)的豁免管理规定,选用磷酸盐组合药剂和硫基螯合剂对飞灰进行重金属稳定化实验,考察了2类药剂对飞灰重金属的稳定效果.寻求达到最佳重金属稳定效果的药剂添加量,同时分析了稳定化飞灰进入生活垃圾填埋场时初期渗滤液中的重金属浸出情况.结...     

有机磷酸HEDP稳定垃圾焚烧飞灰重金属的研究

研究了有机磷酸羟基亚乙基二膦酸(HEDP)对生活垃圾焚烧飞灰中重金属的稳定方法.通过对不同HEDP投加量处理后的飞灰试样作危险废物浸出毒性鉴别试验,分析HEDP最佳使用剂量,并评价了稳定化飞灰的长期稳定性.结果表明,HEDP最适使用剂量为0.03 Ml/g(以商品级HEDP与飞灰的体积质量比计),处理后飞灰与原状飞灰相比,Pb、Zn和Hg的浸出浓度分别降低了98.3%、99.5%和85.0%.HEDP对飞灰中重金属稳定效果排序为:Pb＞Zn＞Hg＞Ni＞Cu＞Cd＞CrHAs.重金属pH相关浸出测试(pH-dependent leaching tests)表明:经0.03mL/g HEDP稳定处理的飞灰,在0.3 mol/L HNO3和0.3 mol/L NaOH的浸取条件下,其重金属浸出浓度均低于国家危险废物鉴别标准,显示具有良好的长期稳定性.     

新型重金属螯合剂对焚烧飞灰中Pb的稳定性能研究

生活垃圾焚烧飞灰因富集重金属，需稳定化处理后填埋处置。采用新型重金属螯合剂(0代端二硫代羧酸基聚酰胺-胺超支化聚合物(PAMAM/4DTC-0G))、二甲基二硫代氨基甲酸钠(SDD/DTC)和乙二胺-双二硫代氨基甲酸钠(EDA/2DTC)对Pb浸出浓度较高的飞灰进行稳定化处理，考察螯合剂投加量、浸出液pH对其稳定化效果的影响，并通过Pb形态分布、红外吸收光谱和微观形貌表征探究稳定化机理。结果表明，2%(质量分数，下同)的PAMAM/4DTC-0G能使飞灰中Pb的浸出浓度低于《生活垃圾填埋场污染控制标准》(GB 16889—2008)限值；5%的PAMAM/4DTC-0G稳定化后的飞灰中Pb的浸出浓度在较宽的pH范围(2～14)内均低于标准限值；PAMAM/4DTC-0G可与Pb²⁺结合形成超大三维网络状螯合物，能实现长期稳定。     

垃圾焚烧飞灰重金属稳定化药剂处理效果

根据某有机螯合剂、硫化钠、磷酸钠、磷酸氢二钠、碳酸钠和硫代硫酸钠6种化学稳定剂对重金属元素稳定化效果的比较结果,并针对重庆飞灰中Pb和Cd浸出浓度超过GB 16889-2008限值0.25 mg/L和0.15 mg/L的情况,选择合适的药剂配伍和剂量对重庆飞灰进行稳定化处理。按照飞灰中重金属含量的不同,对武汉、重庆和成都三地的飞灰进行不同剂量的稳定剂添加实验。结果表明,有机螯合剂、硫化钠、磷酸钠3种化合物对Pb和Cd均有优异的稳定化效果。在有机螯合剂∶硫化钠/磷酸钠质量比为1∶1,2∶1和4∶1的6种配伍稳定化实验中,有机螯合剂∶硫化钠质量比为4∶1的稳定剂配比对重庆飞灰中重金属进行稳定化处理效果最好。研究还发现,使用2倍理论量的有机螯合剂和硫化钠能分别经济有效地完成对武汉、重庆和成都飞灰中重金属的稳定化处理。     

有机螯合剂与磷酸盐联合稳定垃圾焚烧飞灰中重金属的作用机理

为探讨二硫代氨基甲酸型有机螯合剂(FACAR)和重过磷酸钙(TSP)对垃圾焚烧飞灰中重金属Pb、Cd、Ni的稳定作用机制,对稳定前后的飞灰采用BCR连续提取法、 X射线衍射(XRD)分析以及扫描电镜-能谱(SEM-EDS)联用等分析方法进行了表征。结果表明:投加质量分数5%的FACAR能有效稳定飞灰中Pb、Cd和Ni,其浸出浓度低于《生活垃圾填埋场污染控制标准》(GB 16889-2008)规定的浸出浓度限值;采用3%FACAR和3%TSP复配药剂处理,可使飞灰达到GB 16889-2008进场要求;经复合药剂稳定处理后的飞灰颗粒表面孔隙度明显降低,飞灰中Pb、Cd和Ni的形态均由不稳定态向稳定态转化。该复合稳定剂的稳定机制主要为螯合、共沉淀和吸附联合作用机制,其中,有机螯合剂中含硫官能团是影响重金属稳定的主要因素,且重金属具有优先与含硫官能团结合的特性。     

危险固体废物焚烧残渣的稳定化处理研究

采用常规危险固体废物稳定剂Na3 PO4、Na2S、腐殖酸以及工业固体废物电石渣对台州典型危险固体废物焚烧残渣进行稳定化处理.以残渣中污染最严重的重金属Pb、Ni、Cu、Zn的去除率为衡量指标,进行稳定化时间优化试验.结果表明,Na3 PO4、电石渣可在7d后达到较好的稳定化效果,且随着时间的延长效果稳定；而Na2S和...     

不同方法处理飞灰对亚甲基蓝的吸附性能

为了研究不同方法处理飞灰对亚甲基蓝的吸附性能和吸附上清液中重金属的浸出毒性,分析了水洗、硫酸洗和醋酸洗飞灰及在吸附过程中投加NaOH和Na2 CO3对亚甲基蓝的吸附效果的影响,以及吸附上清液中Pb和Cr的浸出情况.实验得出,不同方法处理飞灰对亚甲基蓝的脱色率均达70％以上,最高可达100％,通过水洗和酸洗,飞灰的稳定性显著提高,1％硫酸和5％醋酸洗飞灰吸附上清液中Pb和Cr的浸出量远远低于《危险废物鉴别标准浸出毒性鉴别》的限定值.飞灰经过稳定化处理,用以处理染料废水具有巨大潜能.     

SGA对垃圾焚烧飞灰中重金属的固化性能研究简

根据EPA 1311、HJ/T 299-2007、HJ/T 300-2007和HJ 557-2009等国内外不同标准，研究了深圳某垃圾焚烧发电厂垃圾焚烧飞灰的浸出毒性，探讨了六硫代胍基甲酸（sixthio guanidine acid，SGA）、二甲基二硫代氨基甲酸盐（sodium dimethyl dithio carbamate，SDD）和Ca（OH）₂浓度对垃圾焚烧飞灰中重金属的固定性能的影响。研究结果表明，随着浸提液pH的降低，该厂焚烧飞灰中大部分金属元素的浸出量增大，焚烧飞灰浸出液中的Cd、Ni、Pb和Zn浓度分别超过国家危险废物鉴别标准（GB5085.3-2007）规定值的4.75倍、1.47倍、6.72倍和2.20倍，属于危险废弃物，必须进行稳定化处理。当固化剂SGA加入量为0.1 mol/kg时，稳定化后的重金属浸出浓度已经低于危险废物鉴别标准，且对Cd、Cr、Cu和Pb的固化性能优于SDD和Ca（OH）₂；当固化剂SGA、SDD和Ca（OH）₂加入量为0.5 mol/kg时，稳定化后的焚烧飞灰重金属浸出浓度均低于国家危险废物鉴别标准（GB 5085.3-2007）中的规定值。与SDD和Ca（OH）₂相比，SGA对垃圾焚烧飞灰中重金属的固化处理更具有优势。     

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.