城市生活垃圾焚烧处理过程中重金属迁移规律研究

通过采集厦门2个垃圾焚烧发电厂进厂垃圾、渗滤液、飞灰、炉渣和烟气样品,分析垃圾组成成分及各组分的重金属含量,结果表明,垃圾中以厨余、橡塑类和纸类为主,共占到垃圾干基的78．08％,重金属含量大小次序为Zn〉Cu〉Pb〉Cr〉Ni〉Cd〉Hg;垃圾渗滤液中除Zn外,其他金属的含量都较低,一厂渗滤液中重金属Ni、Zn迁移量较大,分别达到24．46％和8．52％。二厂渗滤液中重金属的迁移有相同的趋势,但含量相对较高。垃圾焚烧后其重金属主要分布在飞灰和废渣中,烟气中的含量非常少,不同金属的含量均有差别,这与金属的性质有很大关系;通过浸出毒性分析,飞灰中重金属酸溶态含量多,容易浸出,属于危险废物。同时,不同烟气处理工艺产生的飞灰的重金属浸出量有很大差别。     

垃圾焚烧过程中影响重金属分布因素的研究

在转式垃圾焚烧炉和固定床加热炉中,研究了有机垃圾焚烧过程中温度、水分、无机氯及有机氯对几种重金属分布的影响。研究结果表明,焚烧垃圾过程中焚烧温度对重金属分布特性的影响特性不一,重金属锌和铅容易转移到气相中去,而重金属镍和铬大部分是以固态形式残留在底渣中;水能与重金属及其化合物发生反应,引起物质转变,影响重金属的分布;氯的存在也影响重金属的分布特性,氯的参与使重金属更易向飞灰或烟气中迁移。     

垃圾焚烧电厂烟气降温模拟分析

采用fluent软件对江苏某垃圾焚烧厂的烟气2级喷水减温流程分别进行了模拟,并根据模拟结果分析了反应塔和冷却塔内烟气的温度、流速、湿度等在塔内的径向分布情况.结果表明,冷却塔和反应塔在不同进口烟气温度下将烟气温度降低到各自相应同一值时所需喷水量的模拟值和实际值均具有较好的一致性,模拟结果具有一定的可靠性;冷却塔内烟气温...     

垃圾焚烧飞灰中的重金属污染物处理方法

随着垃圾焚烧技术在各个城市生活垃圾处理中的广泛应用,对生活垃圾焚烧的残余物,主要是飞灰的处理、处置,已成为困扰人们生产生活的重要难题之一。飞灰的处理是控制重金属污染的关键,目前处理垃圾焚烧飞灰中重金属污染物的常用方法有：水泥固化法、化学药剂稳定法、飞灰热处理、化学浸提法等,生物淋滤法是近年新兴起来的金属浸提技术。经处理后的飞灰可进行填埋或资源化利用。因此,着重叙述了当前有关垃圾焚烧飞灰中重金属污染的控制方法与处置技术的研究现状。     

燃煤电厂重金属排放与周边土壤重金属污染评价

为研究燃煤电厂重金属排放对周边土壤重金属污染的影响,测定了某燃煤电厂烟囱入口烟气中Cd、Cr、Hg、Ni、Pb、As含量,同时根据当地气象及地形条件,在燃煤电厂周边采集19个土壤样品,分析了土壤中重金属含量及分布情况,并对其污染程度进行评价.结果表明,燃煤电厂烟气中6种重金属元素的质量浓度为0.02～2.00μg/m3...     

掺加矿粉胶凝固化垃圾焚烧飞灰中重金属的研究

通过单因素实验探究了矿粉质量分数、激发剂(NaOH)投加量和加水量对掺加矿粉胶凝固化垃圾焚烧飞灰中重金属的影响,并初步探究了固化机理。结果表明,矿粉质量分数和激发剂投加量对重金属的固化影响较大,而加水量影响不大。综合考虑增容比、重金属浸出浓度和抗压强度,矿粉质量分数15%、激发剂投加量3%(质量分数)、加水量37.5%(质量分数)为有效稳定固化重金属的最佳条件,此时重金属浸出质量浓度分别是Ba 19.091mg/L、Cd 0.041mg/L、Ni 0.216mg/L、Pb 0.196mg/L,含水率为27.04%,满足《生活垃圾填埋场污染控制标准》(GB 16889—2008),抗压强度为9.61 MPa,可进入垃圾填埋场填埋。所制备胶凝材料的最终水化产物主要为水化硅酸钙、水化铝硅酸钙和钙矾石,它们可以通过包裹和吸附对重金属进行固化。     

垃圾焚烧飞灰有毒重金属固化稳定技术研究综述

采用焚烧法处理生活垃圾正呈快速增长的趋势,焚烧过程产生的飞灰中所含有的大量有毒重金属对自然环境和人类生存都造成极大影响。阐述了目前常用的几种固化稳定垃圾焚烧飞灰有毒重金属的方法,综合分析了其固化特点和优缺点,并初步探索了一种低能耗环境下实现高温熔融处置技术的有效途径,从而为垃圾焚烧飞灰高温固化稳定有毒重金属的实施提供一定的理论基础和技术支持。     

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.     

垃圾焚烧过程中影响重金属分布因素的研究

在转式垃圾焚烧炉和固定床加热炉中，研究了有机垃圾焚烧过程中温度、水分、无机氯及有机氯对几种重金属分布的影响。研究结果表明，焚烧垃圾过程中焚烧温度对重金属分布特性的影响特性不一，重金属锌和铅容易转移到气相中去，而重金属镍和铬大部分是以固态形式残留在底渣中；水能与重金属及其化合物发生反应，引起物质转变，影响重金属的分布；氯的存在也影响重金属的分布特性，氯的参与使重金属更易向飞灰或烟气中迁移。     

基于重金属提取的垃圾焚烧飞灰无害化处理

采用加酸浸出工艺对垃圾焚烧飞灰进行无害化处理。研究证明盐酸能有效分离飞灰中重金属,重金属浸出率与盐酸浓度及液固比有关;重金属在实验的盐酸浓度和液固比下都能达到高浸出率,但液固比越低,浸出液中重金属的浓度就越高,越有利于重金属的回收。当盐酸浓度为5 mol·L-1、液固比为2（mL:g）时,Pb、Cd和Zn浸出率均达到95%以上,而Cu的浸出率也达到81.38%,Pb、Cd、Zn和Cu的浓度分别为468.10、78.12、2 268.80和347.78 mg·L-1。残灰采用加盐水洗工艺后,浸出毒性超标的重金属Pb和Cd浸出毒性低于GB 16889-2008标准限值,符合填埋要求。     

城市垃圾焚烧渗沥液中Ca2＋对厌氧EGSB处理效果的影响

研究了城市生活垃圾焚烧厂渗沥液中Ca2＋对厌氧颗粒污泥膨胀床反应器（EGSB）处理效果的影响,并采用静态实验方法考察了Ca2＋对厌氧颗粒污泥产甲烷活性的影响。实验结果表明,进水COD为17000mg／L的条件下,当Ca2＋浓度低于6000mg／L时,EGSB对COD去除率达93％以上;当Ca2＋浓度高于6000mg／L时,COD去除率随运行时间明显下降,并在污泥中形成大量沉淀。静态实验结果表明,废水中低浓度Ca2＋促进了厌氧颗粒污泥的产甲烷活性,但高浓度Ca2＋明显抑制了其产甲烷活性,这是导致高Ca2＋浓度条件下EGSB对COD去除率降低的主要原因。研究表明,颗粒污泥产甲烷活性恢复程度随Ca2＋浓度增加而减弱。     

医疗垃圾焚烧飞灰重金属形态分析

利用原子吸收光谱仪分别对医疗垃圾焚烧飞灰重金属含量和重金属形态及其随颗粒度分布特性进行了分析,结果表明,飞灰中Cd、Zn、Pb等的浸出浓度远超标与这些重金属的可交换态和碳酸盐态含量较高有关;飞灰颗粒度主要在96 μm以下,96～150 μm的颗粒中Cd、Pb含量最高,且Zn、Cd的形态以可交换态为主.     

湿解焚烧综合处理垃圾技术的原理及应用

详细介绍了湿解焚烧处理生活垃圾技术的原理和其在武汉经济技术开发区的具体应用，并简述了其在一段时间的调试和运行后表现出的优点。为国内未来垃圾气化熔融焚烧技术的推广提供了参考。     

不同城市生活垃圾焚烧技术的综合评价

通过工程的经济性分析、工艺过程的能流分析以及工程的环境影响分析,综合分析了流化床、炉排炉、气化熔融和等离子体气化等不同城市生活垃圾焚烧技术。结果表明:(1)在零补贴的情况下,流化床焚烧技术的工程效益最佳,但从项目投产年算起,其投资回收期也需9年;炉排炉、气化熔融与等离子体气化焚烧技术要达到流化床焚烧技术零补贴情况下的经济效益,分别需补贴约70、140、500元/t。(2)各城市生活垃圾焚烧技术下区域的水体富营养化和全球变暖影响最显著,而人体毒性影响最小。气化熔融焚烧技术和等离子体气化焚烧技术的环境影响比其他两种焚烧技术小一个数量级。(3)考虑污染物排放的环境效益,在现行中国排放标准下,流化床、炉排炉与气化熔融焚烧技术的工程效益都将得到较大提升。随着排放标准的更加严格,流化床焚烧技术的年收益率下降最显著;气化熔融焚烧技术的工程效益相较最优。     

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...     

Polycyclic aromatic hydrocarbon emissions from clinical waste incineration

Since the introduction of the Environmental Protection Act in the UK, there are few reports of PAH emissions from clinical waste incinerators (CWIs) operating to improved performance standards. The main aim of this study is to determine PAH emissions from a state-of-the-art CWI focusing on the effects of reactive gases and operating variables on emissions. This was carried out by collection of stack samples over three phases of operation.

At stack conditions, most PAHs are predicted to be in the vapour phase. Reactive losses of PAHs were closely correlated by rank with expected reactivities from laboratory studies. Estimates of emissions incorporating sampling losses were derived, although no correlation was found between PAH losses and the modest levels of reactive stack gases. PAH concentrations were one to two orders of magnitude lower than earlier reports from incinerators without effective air pollution control equipment (APCE). The low levels of carbon monoxide recorded were not correlated with any PAHs.

This study demonstrates the impact of efficient combustion conditions and APCE on PAH emissions from a CWI.     

Bromine in waste incineration partitioning and influence on metal volatilisation

INTENTION, GOAL, SCOPE, BACKGROUND: The halogen bromine is far less abundant than chlorine, but it can be found at high concentrations in special materials like flame retarded plastics. The fate and effects of Br in waste incineration are not well understood. It may have similar implications like Cl for the volatilisation of heavy metals and the formation of low volatile organic compounds. Due to its lower oxidation potential, there is a risk of formation of elementary Br2 in the offgas. OBJECTIVE: Co-combustion tests of different types of Br containing plastic waste materials (up to 22%) and MSW in the TAMARA pilot plant for waste incineration were conducted to investigate the Br partitioning and the influence of Br on metal volatilisation. METHODS: The Br inventory of the fuel mix was elevated to approx. 1 wt-%. All input and output mass flows of the furnace have been sampled and the partitioning of Cl, Br, S, and a number of heavy metals, has been calculated on the basis of closed mass balances. RESULTS AND DISCUSSION: Organically-bound Br was typically released to more than 90% into the raw gas. Elementary Br2 was detected at high Br levels. Its presence was always analysed when all SO2 in the raw gas was oxidised to SO3. Br enhances the volatilisation of metals like K, Zn, Cd, Sn, Sb, and Pb out of the fuel bed principally in the same way as Cl. The tests gave strong indication that the promoting influence of the halogens on metal volatilisation is more pronounced than that of the fuel bed temperature. The volatilised metals are condensated on the fly ashes and are discharged along with the filter ashes. CONCLUSIONS: As long as a surplus of SO2 is present in the raw gas no Br2 is formed. Although the halogen induced transfer out of the fuel bed causes high concentrations of volatile metals in the filter ashes, a recovery is not economically feasible for the time being. The volatilisation gives no rise to metal emission problems as long as efficient dedusting is achieved. RECOMMENDATION AND OUTLOOK: If there is a risk of Br2 formation, in wet scrubbing a reducing agent has to be added to the neutral scrubber for efficient abatement. Filter ashes should be disposed of in a way that enables access for recovery in the future. The exact volatilisation characteristics of the various metals have to be studied in future using specifically tailored experiments.     

城市生活垃圾和污水处理厂剩余污泥混合发酵的原料配比优化研究

以城市生活垃圾和污水处理厂的剩余污泥为混合原料,研究了混合原料的不同配比对厌氧发酵过程及产气的影响。结果表明:城市生活垃圾与剩余污泥以挥发性固体(VS)质量比为2∶1混合后,厌氧发酵效果最好,累计产气量最高,达到8 721mL,发酵后的总固体(TS)、VS、COD去除率分别达43.65%、35.98%、47.88%;各实验组在发酵过程中的pH、氨氮浓度和碱度均在合理范围内,未对厌氧发酵反应造成影响;以适当配比的城市生活垃圾和剩余污泥为混合原料,进行中温联合厌氧发酵是可行的,联合厌氧发酵可以弥补单一原料的缺陷,在一定程度上改善厌氧发酵效果。     

Assessment of polychlorinated dibenzo-p-dioxin and dibenzofuran emissions from a hazardous waste incineration plant using long-term sampling equipment

The aim of this work is to evaluate the performance of a continuous monitoring system for the analysis of the mass concentration of PCDD/Fs from stationary sources. Data was acquired from a modern, state of the art, hazardous waste thermal treatment plant for a period of more than 2 years using a commercial available continuous monitoring system. The study consisted of a total of 16 samples, collected in periods from 1 week to 2 months resulting in an average of 360 m³ sampled flue gas per sample. The study showed the system was able to confirm that for a period of more than 2 years the plant was complying with the limit of 0.1 ng I-TEQ/Nm³. In addition, the data showed the typical fingerprint of such installations which is useful for example in impact studies. Long-term samples were compared to five short-term samples (6 h) collected every 6 months during the study period. Principal component analysis was applied to PCDD/Fs obtained data as useful statistical tool to find out trends and similarities between different samples. Improvement in terms of representativeness of data was achieved through continuous assessment since the starts of the project. The obtained data was further used to determine the emission factor for this activity and the total annual PCDD/Fs release to the atmosphere.