氧化铜催化五氯苯生成二噁英的研究

研究在加热条件下,五氯苯在CuO表面催化生成二噁英(PCDD/Fs)的过程.结果表明,在200～350℃,PCDD/Fs的生成量随温度的升高而增加;在350～450℃,PCDD/Fs的生成量随温度的升高而减少.温度较低时(200～250℃),生成的PCDD/Fs以高氯取代同系物为主;温度较高时(400～450℃),则以低氯取代的同系物为主.但温度的改变并没有引起同一氯取代度PCDD/Fs中的异构体分布模式发生规律性变化.通过比较400℃条件下CuO催化五氯苯生成PCDD/Fs与CuO催化OCDD/F的脱氯降解情况,推测了五氯苯生成PCDD/Fs的途径.低氯取代的PCDDs可能主要来源于五氯苯生成的高氯取代PCDDs的进一步脱氯降解.而PCDFs则主要由五氯苯脱氯降解生成的低氯取代产物直接缩合生成.     

飞灰中二英热脱附行为的研究

研究了垃圾焚烧产生的飞灰中二噁英在隔绝空气受热条件下的热脱附行为及规律.通过气相和固体残留中二噁英的含量分析,推测了二噁英在不同温度条件下可能发生的几种化学反应和物理变化,同时研究了17种有毒二噁英的热脱附效率和飞灰的最佳热脱附条件.PCDD/Fs在200℃和300℃下平均脱附率分别为96.2%和95.5%,而400℃下的平均脱附率高达99.7%.结果表明,在300℃加热条件下,飞灰中的PCDD/Fs主要发生脱氯降解反应.在400℃下,飞灰中发生大量的前体合成反应,使PCDD/Fs含量显著增加.     

废物焚烧厂烟气中PCDD/Fs和PCNs的排放特征

采用同位素内标稀释高分辨气质联用分析法,对废物焚烧厂的烟气样品PCDD/Fs和PCNs进行了测定,分析了其排放特征以及相关性,为有组织排放的PCDD/Fs和PCNs的控制提供理论依据.实验结果表明,空白实验中未发现明显的背景干扰;样品中PCDD/Fs的采样内标回收率范围为74.0%~90.1%,提取内标的回收率范围为53.3%~120.0%,均符合US EPA23和CHN HJ77.2-2008的质量控制标准;PCDD/Fs的同系物浓度均随着氯取代数目的增加而增加,而PCNs同系物则随着氯取代数目的增加表现出先增大后减小的规律.同系物之间的皮尔森相关系数分析结果可知,这两类污染物相邻同系物相关性系数明显大于非相邻同系物相关性系数,表明低氯代同系物可能是生成高氯代同系物的一个重要途径.此外,PCNs和PCDD/Fs同系物的线性相关分析结果表明,一些PCNs化合物（PeCN、HxCN、HpCN、OCN）与某些PCDD/Fs（OCDD、PeCDF、HxCDF、HpCDF）具有良好的相关性（R²=0.55~0.78）,由此推断在废物焚烧过程中这些同系物可能具有相类似的生成机制.     

SCR装置对焦炉煤气燃烧废气中PCDD/Fs、PCBs和PCNs的协同脱除

研究了某大型焦化厂的选择性催化还原(SCR)装置对焦炉煤气燃烧废气中典型非故意产生持久性有机污染物(UPPOPs)的脱除效果,对SCR装置入口和出口废气和SCR装置降尘中二英(PCDD/Fs)、多氯联苯(PCBs)和多氯萘(PCNs)的全部异构体进行了分析.结果表明,SCR装置对总PCDD/Fs的脱除效率最高,为94.6%,对总PCBs和总PCNs的脱除率分别为74.7%和78.4%.SCR装置入口和出口废气中UP-POPs同系物的分布模式明显不同,入口处以高氯取代为主,出口处以低氯取代为主.SCR装置对高氯取代UP-POPs有更好的脱除效果.催化还原和催化氧化降解同时发生是SCR装置脱除废气中UP-POPs的重要机制.     

SCR装置对焦炉煤气燃烧废气中PCDD/Fs、PCBs和PCNs的协同脱除

研究了某大型焦化厂的选择性催化还原(SCR)装置对焦炉煤气燃烧废气中典型非故意产生持久性有机污染物(UP-POPs)的脱除效果,对SCR装置入口和出口废气和SCR装置降尘中二噁英(PCDD/Fs)、多氯联苯(PCBs)和多氯萘(PCNs)的全部异构体进行了分析。结果表明,SCR装置对总PCDD/Fs的脱除效率最高,为94.6%,对总PCBs和总PCNs的脱除率分别为74.7%和78.4%。SCR装置入口和出口废气中UP-POPs同系物的分布模式明显不同,入口处以高氯取代为主,出口处以低氯取代为主。SCR装置对高氯取代UP-POPs有更好的脱除效果。催化还原和催化氧化降解同时发生是SCR装置脱除废气中UP-POPs的重要机制。     

贵屿某电子垃圾拆解点附近大气颗粒物中氯代/溴代二噁英、四溴双酚A污染水平研究

对贵屿某电子垃圾拆解点附近大气颗粒物中氯代二英(PCDD/Fs)、溴代二英(PBDD/Fs)、四溴双酚A(TBBPA)含量水平进行了调查研究.结果显示,大气颗粒物中17种2,3,7,8-PCDD/Fs和8种2,3,7,8-PBDD/Fs的浓度范围分别为126.54～524.78pg·m-3和376.42～566.76pg·m-3;平均毒性当量(TEQ)分别为16.29pg·m-3、91.28pg·m-3,均高出目前所报道的国内外其它部分城市大气污染水平1～4个数量级,且PBDD/Fs的污染水平远远高于PCDD/Fs.四氯至八氯代PCDD/Fs同系物呈现出明显且特别的分布规律,PCDDs和PCDFs浓度均随着氯原子取代程度增加而降低.TBBPA的浓度范围为66.01～95.04ng·m-3,大气中PBDD/Fs浓度与之显著相关r=0.69.初步的暴露风险评价表明,当地居民每日通过呼吸摄入的二英含量远远超过了世界卫生组织(WHO)规定的人体每日耐受量(TDI)1～4pg(W-TEQ)·kg-·1d-1.     

氯化铜催化二噁英生成实验及指纹特性分析

氯化铜被认为是对二■英(PCDD/F)生成促进作用最强的金属催化剂,温度和氧气含量是影响其催化二■英生成的关键因素.本文选取250～550℃间8个不同温度点及0～20%间4种不同氧气含量,系统性地研究了温度和氧气含量对含氯化铜模拟飞灰(MFA)生成二■英的影响,并通过分析指纹特性探讨二■英的生成路径和机理.结果发现,290～350℃之间二■英生成量较高,且在290℃时二■英总量达到最大值;氧气含量为10%时二■英生成量达到最高.研究二■英同分异构体分布可从分子层面为研究其生成路径和机理提供重要信息,因此,本文分析了四至八氯代PCDD/F的全部异构体的分布.结果表明,在本文所选取的温度和氧含量范围内,温度对二■英生成路径的影响高于氧气含量.最后,重点讨论了2,3,7,8位氯取代的17种有毒异构体的分布随温度和氧气的变化情况及生成路径.利用主成分分析法(PCA)证实了氯化铜催化二■英从头合成过程中存在经由氯酚路径生成的异构体,并讨论了不同工况下氯酚路径对二■英生成的影响.     

再生铝?铅生产企业PCDD/Fs排放浓度与特征

研究了国内3家再生金属企业排放烟气和飞灰中PCDD/Fs排放浓度和同系物分布特征,其中两家再生铝企业?一家再生铅企业.研究结果显示:两家再生铝企业排放烟气中PCDD/Fs毒性当量浓度( I-TEQ)分别为2.14和0.88ng TEQ/Nm3,飞灰中分别为33.90和0.77ng TEQ/g;再生铅企业排放烟气和飞灰中PCDD/Fs毒性当量浓度分别为0.037ng TEQ/Nm3和0.014ng TEQ/g;两家再生铝企业排放烟气中PCDD/Fs同族体分布存在较大差异,而飞灰中PCDD/Fs同族体分布却十分相似;再生铅?铝企业排放的PCDD/Fs同系物分布特征差异较明显;且根据PCDFs与PCDDs总浓度比值大于1可以判断,二者排放PCDD/Fs的形成机理都以从头合成为主.     

蚀刻废液及其回收后生产的铜盐产品中PCDD/Fs含量水平及分布特征

通过高分辨气相色谱-高分辨磁质谱联用仪(HRGC-HRMS)测定了蚀刻废液及其回收利用后生产的铜盐产品中17种2,3,7,8取代PCDD/Fs的浓度.结果表明,蚀刻废液中PCDD/Fs浓度范围为0～3 460 pg·L-1,平均值为616 pg·L-1,毒性当量浓度WHO-TEQ范围为0～246 pg·L-1,平均值为42.9 pg·L-1;铜盐产品中PCDD/Fs浓度范围为1.08～24.6 ng·kg-1,平均值为8.83 ng·kg-1,毒性当量浓度WHO-TEQ范围为0.112～0.715 ng·kg-1,平均值为0.338 ng·kg-1.通过净化处理工艺可以除去蚀刻废液中大部分PCDD/Fs.在蚀刻废液生产的各级产品中,工业级产品中PCDD/Fs浓度高于饲料级与电镀级产品.各铜盐产品中PCDD/Fs具有相似的单体分布特征:①PCDFs的百分含量明显高于PCDDs;②除硫酸铜类产品中的2,3,7,8-TCDF外,单体的氯取代数越大,百分比含量越高.     

《火葬场大气污染物排放标准》实施对火化炉烟气二噁英减排的影响

为调查殡葬行业大气污染物排放新标准《火葬场大气污染物排放标准》(GB 13801—2015)实施4年后火化烟气中二英(PCDD/Fs)的污染排放特征及其对行业的影响,在我国南方地区选取了32台火化炉,对其排放烟气中PCDD/Fs水平、影响因素、排放因子进行了研究,并评估标准实施4年后的效果. 结果表明:①火化烟气PCDD/Fs毒性当量浓度(以I-TEQ计,下同)为0.033~7.4 ng/m3,平均值为1.1 ng/m3,PCDD/Fs超标率为56.2%,其中拣灰炉和平板炉超标率分别为62.5%和50.0%. 与GB 13801—2015实施前相比,火化炉废气中PCDD/Fs排放浓度显著下降,说明PCDD/Fs污染减排成效明显,但排放水平和超标率仍较高. ②有无废气处理工艺、运行管理水平、随葬品数量与PCDD/Fs排放浓度密切相关. 废气处理设施缺失或无法正常运行时PCDD/Fs毒性当量浓度为0.32~7.4 ng/m3,平均值为2.5 ng/m3,超标率达75.0%;配备“活性炭吸附(ACI)+布袋除尘(BF)”工艺且运行正常时,PCDD/Fs毒性当量浓度范围为0.033~4.5 ng/m3,平均值为0.83 ng/m3,超标率为58.3%,可能与部分处理设施使用率低、运行不佳和维护不到位等原因有关. 指纹特征显示,无废气处理工艺时七氯代、八氯代同系物占比较高;配备“ACI+BF”处理设施时以四氯代、五氯代同系物为主,证实该工艺组合主要去除高氯代同系物. ③火化炉废气PCDD/Fs排放因子(以I-TEQ计,下同)为67.8~39 981 ng/具,平均值为4 217 ng/具,显著低于联合国环境规划署(UNEP)于2005年发布的第1和第2级排放因子(分别为90和10 μg/具),但高于其优化控制措施的排放因子(0.4 μg/具). 研究显示,未来需加强对我国遗体火化PCDD/Fs减排的技术帮扶及排放因子的更新.      

医疗废物焚烧飞灰二英的热处理研究

比较了医疗废物焚烧飞灰在温度200～450℃,流动氮气和静态空气气氛中二(噁)英气固相行为变化.在流动氮气条件下,固相二(噁)英随温度升高逐渐增加,350下飞灰二(噁)英浓度升至最高,毒性当量浓度和总浓度分别增加了46.0%和26.0%,随后随着温度升高,二(噁)英含量逐渐降低,450℃条件下浓度减少至最低,分别减少了86.8%和80.5%.在静态空气下,固相二(噁)英随温度至250℃条件下,飞灰二(噁)英浓度升至最高,毒性当量浓度和总浓度分别增加了20.7%和28.7%,随着温度进一步升高,二(噁)英含量逐渐降低,450℃条件下浓度减至最低,分别减少了99.5%和99.5%.气相只有少量二(噁)英产生,仅占总产生量的0.11%～2.16%.本实验研究飞灰的最佳热处置条件为:静态空气条件下,450℃处置1 h.本研究中,分解反应在PCDDs与PCDFs的降解过程起到主要作用,而脱氯与脱附仅为次要作用.     

Effects of inorganic chlorine source on dioxin formation using fly ash from a fluidized bed incinerator

Chlorine source is indispensable for polychlorinated dibenzo-p-dioxin and furan (PCDD/F) formation during municipal solid waste (MSW) incineration. Inorganic chlorine compounds were employed in this study to investigate their effects on PCDD/F formation through heterogeneous synthesis on fly ash surfaces. A fly ash sample obtained from a fluidized bed incinerator was sieved to different size fractions which served as the PCDD/F formation sources. The capability of different metal chlorides which facilitate the formation of PCDDs/Fs was found to follow the trends: Na ＜ Mg ＜ K ＜ Al ＜ Ca, when two particle fractions of ＞177 μm and 104-125 μm were used in the experiments. However, the capability of NaCl, MgCl2 and KCl did not seem much different from each other, whereas CaCl2 and AlCl3 were much more active in PCDD/F formation. NaCl and MgCl2 were relatively effective to produce more PCDDs, while KCl, AlCl3 and CaCl2 generated more PCDFs during heterogeneous reactions occurring on fly ash. 2,3,7,8-TCDF was the most significant contributor to the toxicity of the PCDDs/Fs formed from inorganic chlorine sources. Decreasing the sizes of fly ash particles led to more active formation of PCDDs/Fs when NaCl was used as inorganic chlorine in the experiment. The highest PCDDs/Fs produced from particles with size ＜37 μm, while the lowest PCDDs/Fs produced from particles with size ＞177 μm. The toxicity generally increased with decreasing size of the fly ash particles. The formation of PCDDs was mainly facilitated by the two size fractions, 104-125 μm and ＜37 μm, while formation of PCDFs was favored by the two other size fractions, ＞177 μm and 53-104 μm.     

Effect of temperature and oxygen on the formation of chlorobenzene as the indicator of PCDD/Fs

Sampling and analysis of polychlorinated dibenzo-p-dioxins and dibenzofurans(PCDD/Fs) are both time-consuming and expensive. In principle,real-time monitoring of chlorobenzene(CBz) as an indicator for PCDD/Fs could be useful to control and optimize incinerator operating conditions.To test this strategy,CBz was analyzed together with PCDD/Fs in flue gas samples collected from a hospital waste incinerator.Moreover,lab experiments were conducted to investigate the eect of temperature and oxygen on CBz formation from fly ash from the same incinerator.The experimental results demonstrate that chlorobenzene(in particular PeCBz) correlate well with PCDD/Fs,in line with previous research.The optimum temperature of CBz formation is in a range of 350 to 400°C and CBz yield increases significantly with oxygen,in line with PCDD/Fs formation.This study is useful for confirming the de novo mechanism and defining correlations between CBz and PCDD/Fs.     

Destruction of PCDD/Fs by gliding arc discharges

PCDD/Fs have been become a serious issue because of their toxicological effects and associated adverse health implications.In this study,the gliding arc plasma was tested for treatment of polychlorinated dibenzo-p-dioxins(PCDDs)and polychlorinated dibenzofurans (PCDFs),which was synthesized from pentachiorophenol in atmospheric condition at 35℃with or without the catalysis of CuCl_2. From the experiment,we found that the destruction efficiency of PCDD/F homologues after gliding was discharge ranged from 25% to 79%.This result demonstrates that gliding arc plasma is an effective technology to decompose PCDDs/Fs in flue gas.A plausible degradation mechanism for PCDD/Fs by gliding arc was discussed.Finally,a multistage reactor structure of gliding arc was proposed to upgrade removal efficiency for PCDD/Fs.     

Experimental and modeling study of de novo formation of PCDD/PCDF on MSW fly ash

The effect of sulfur dioxide （SO2） on the formation of polychlorinated dibenzo-p-dioxins （PCDDs） and polychlorinated dibenzofurans （PCDFs） has been studied in an entrained-flow reactor （EFR） under simulated waste combustion conditions. A chlorination model based on conditional probability was employed to evaluate the homologue patterns of PCDDs and PCDFs. Results revealed that the presence of SO2 did not alter the formation pathway although SO2 suppressed PCDD/F formation. The prediction model of PCDF showed good agreement with the experimental data （R--0.95）, whereas the prediction for PCDDs did not correlate well with the experimental data. This may be explained because potential chlorination pathways play a significant role in PCDF formation, whereas PCDDs are mainly formed through condensation reactions. Furthermore, the result indicated that the steric hindrance during formation has more effects on PCDD than on PCDF due to the symmetric molecular structures of PCDDs.     

Removal of PCDD/Fs and PCBs from sediment by oxygen free pyrolysis

Few studies have dealt on the evaluation of volatilization and decomposition reactions of dioxins from sediment by oxygen free pyrolysis. In this study, the performance of pyrolysis on the removal of dioxins from sediment was investigated. Dioxin concentrations of the raw sediment and the solid residues after pyrolysis were analyzed at different conditions. Results showed a removal efficiency of 99.9999% for total dioxins at 800℃ and retention time of 30 min. All the polychlorinated dibenzo-furans （PCDFs） have been removed and were not formed in the solid residues at the retention time range of 30-90 min at 800℃. Close to 100% removal of polychlorinated dibenzo-p-dioxins （PCDDs） was also achieved. Only trace PCDDs were detected in the solid yields at a retention time of 60 min. The highest removal efficiency of polychlorinated biphenyls （PCBs） was more than 99.9994% at a retention time of 30 min. During cooling period following pyrolysis, however, the concentration of total dioxins in solid residues increased 130 times as compared to that of the raw sediment under air atmosphere. This confirmed that some complex reactions do occur to form PCDD/Fs and PCBs from 800 to 400℃ in the presence of oxygen. Oxygen-free atmosphere therefore can prevent formation of dioxin during thermal process thus generating clean solid residues.     

垃圾焚烧飞灰或炉渣中二噁的分布特征

分别采集了3种生活垃圾焚烧炉产生的飞灰或熔融炉渣样品,分析了其中的二口恶口英含量及其毒性当量,并讨论了17种2,3,7,8位氯取代的二口恶口英分布特征及其对总毒性当量的贡献.结果表明,机械炉排焚烧炉产生的飞灰中二口恶口英最多,总浓度为319ng/g,毒性当量为6.7ngI-TEQ/g;其次为流化床焚烧炉,产生的飞灰中二口恶口英总浓度为38.7ng/g,毒性当量为0.8ngI-TEQ/g;气化熔融焚烧炉产生的熔融炉渣中二口恶口英很少,总浓度为38.7pg/g,毒性当量仅为1.1pgI-TEQ/g;所有的2,3,7,8位氯取代的13C同位素标记内标化合物回收率在39%~156%之间.尽管不同的垃圾焚烧炉在二口恶口英的生成量上有明显的差别,但是产生的二口恶口英同类物的归一化浓度以及对毒性当量贡献的归一化结果分布特征十分相似,表明3种垃圾焚烧炉在垃圾焚烧过程产生二口恶口英可能具有相似的反应机理.     

Operating condition influences on PCDD/Fs emissions from sinter pot tests with hot flue gas recycling

This study was designed to clarify the influence of operating conditions on the formation and emissions of polychlorinated-pdibenzodioxins and dibenzofurans (PCDD/Fs) from a sintering process with hot flue gas recycling. A pilot scale sinter pot with simulated flue gas recycling was developed, and four key operational parameters, including temperature, oxygen content of the simulated waste flue gas, the coke rate of the sintering mixture, and the quicklime quality, were selected for exploring PCDD/Fs formation. The results showed that the temperature of the recycled flue gas had a major affect on PCDD/Fs formation, and a high temperature could significantly increase their formation during sintering. A clear linear correlation between the temperature of recycling flue gas and PCDD/Fs emission (r = 0.93) was found. PCDD/Fs could be reduced to a certain extent by decreasing the level of oxygen in the recycled flue gas, while sintering quality was unchanged. The coke rate had no significant influence on the formation of PCDD/Fs, but the quality of quicklime used in the sintering mixture could affect not only the amount of PCDD/Fs emissions but also the sintering productivity. Compared with a benchmark sinter pot test, PCDD/Fs emissions markedly decreased with improvements to quicklime quality. However, the reduction in PCDD/Fs emissions realized by using high-quality quicklime was limited by the temperature of the inlet gas. The highest reduction achieved was 51% compared with conventional quicklime when the temperature of the inlet gas was 150°C.