用光伏污泥焚烧灰渣制备轻集料

针对工业污泥焚烧灰渣处置难的现状,以光伏污泥焚烧灰渣为主要原料制备轻集料。确定轻集料烧制的最佳条件为,黏土投加量为70%,MgO投加量为5%,污泥焚烧灰渣投加量为25%,预热温度为450 ℃,预热时间为15 min,焙烧温度为1 050 ℃,焙烧时间分别为10 min,所制备出的轻集料的抗压强度为9.52 MPa,堆积密度为867 kg·m-3,烧失量为0.12%,1 h吸水率为1.94%。所制得的轻集料强度高,吸水率小,符合《轻集料及其实验方法.第二部分：轻集料实验方法》（GB/T 17431.2-2010）的要求,可为光伏污泥焚烧灰渣资源化提供理论指导。     

燃煤机组电除尘器入口烟道流场优化数值模拟研究

燃煤机组环保设施连接烟道阻力增加是风机能耗增大的主要因素之一,对烟道进行流场优化,降低烟道阻力和风机能耗是燃煤电厂节能降耗的有效途径之一。采用CFD数值模拟对某电厂660 MW燃煤机组电除尘器入口烟道进行流场优化,重点分析了5种不同优化方案下烟道阻力、风机能耗、灰质量流量分配比例、烟气灰浓度、导流板磨损速率等参数的变化规律。结果表明：通过设置合理结构形式及数量的导流板实现烟道降阻幅度28.7%,单台机组最大可节约风机能耗190 kW·h,节能降耗效果显著。新增导流板对烟气中灰质量流量分配比例具有调节作用,优化后A、B两侧烟道内灰质量流量比例偏差由14.8%降低至6.6%,提高了电除尘器的综合除尘率。烟道流场优化在改善灰浓度场分布的同时降低了导流板的磨损,优化后导流板的平均磨损速率由1.33×10⁻⁷ kg/(m²·s)降低至0.56×10⁻⁷ kg/(m²·s),降幅高达57.6%,导流板使用寿命是优化前的2.4倍,提高了机组运行的安全性和可靠性。

     

混合填充体系对铬渣中六价铬的阻留作用

以铬渣和粉煤灰为混合填充体系的主要填料，采用柱子淋洗法，通过改变混合填料的配比来研究其对铬渣中Cr(Ⅵ)的阻留作用。试验结果表明，各种混合填充体系对Cr(Ⅵ)均有一定程度的阻留作用，其中I—5校对Cr(Ⅵ)的阻留固定效果最佳，淋出液中Cr(Ⅵ)的质量分数为0．删％，相对阻留效果达94．53％。     

Drying of granulated wood ash by flue gas from saw dust and natural gas combustion

At the district heating plant of Kalmar, Sweden an on-line unit for production of granulated wood ash for nutrient recycling on forest soils is being applied. Currently, the granules are dried by hot air from an oil-fired burner. The objective of this work was to investigate how drying by flue gas affects the hardening of granules, or impacts their chemical composition and properties. Ninety-six granule samples were treated by flue gas from natural gas combustion in a laboratory pilot scale flue gas generator. CO₂, CO, O₂, C₃H₈ and NO concentrations were varied during the experiment. Additionally, some samples were treated by flue gas from combustion of sawdust at the heating plant in Kalmar. Drying by flue gases did not affect the chemical composition of granules, but minor effects were seen in their mineralogy. The carbonate content was slightly higher in granules treated with flue gas from natural gas combustion compared to the granules dried by hot air only, when measured by wet chemical methods. Results from XRD analysis imply that the calcite content is higher and the portlandite and arcanite content slightly less in granules treated with flue gas from sawdust combustion compared to the granules dried by hot air only. The results from this investigation showed no negative effects on ash granule composition or physical structure by the use of a flue as a drying medium.     

高炉瓦斯泥综合利用技术述评

瓦斯泥是高炉副产物,因其中富含锌,直接用于烧结会增加高炉锌负荷。在分析了瓦斯泥的矿物特征的基础上,综述了选矿法、化学浸出法、直接还原法等几种瓦斯泥有价成分的回收利用方法。选矿法根据碳、锌、铁的性质及赋存状态的差异分离各物质,具有工艺简单、成本低的优点,但分离不彻底、回收率低;化学浸出法使锌进入溶液而其他矿物不溶或微溶,分离效果较好,但处理量小,后续处理难度大;直接还原法是在高温下使瓦斯泥中的金属还原,锌蒸发后进入烟气,最终可得到含氧化锌较高的烟尘和含金属铁的脱锌瓦斯泥,该法适应性强、处理量大、分离效果好,是目前应用较为广泛的瓦斯泥处理方法,但其设备投资大。     

基于国内水泥生产现状的碳排放因子测算

水泥生产过程中碳排放因子的测算是计算水泥碳排放量的基础,为了准确测算我国水泥行业熟料煅烧阶段碳酸盐矿物分解释放CO2的碳排放因子,就需要对水泥生产线上相关样品做成分测定和综合分析.通过对国内近百条代表性较强的水泥生产线上的生料、熟料、水泥、石灰石、燃煤等样品进行钙、镁、烧失量、碳酸盐等化学成分的定量分析,并考虑新型干法窑和立窑两种生产工艺类型的差别,分析测算了基于国内水泥生产的工艺碳排放因子.结果表明:生料碳酸盐法测算碳排放因子的结果较熟料法的结果低约10kgCO2/tcl;不同窑型的碳排放因子存在明显差异,新型干法窑的碳排放因子多集中在500~520kgCO2/tcl,立窑碳排放因子多集中在480~500kgCO2/tcl;多数熟料含有少量碳酸盐.生料碳酸盐法不涉及燃煤灰分的化学成分,可以规避燃煤灰分成分的影响,测算碳排放因子采用生料碳酸盐法较准确,并且应基于不同窑型,同时考虑碳酸盐分解率问题.     

两种粉煤灰的烟气脱硫实验

采用粉煤灰(FA)和Ca(OH)2水合制得的高活性吸收剂作为二氧化硫的干法脱硫剂，重点研究了两种粉煤灰(电除尘灰和湿式水膜除尘灰)在同一配比、同一水合温度、同一水合时间下的脱硫效率，结果表明：电除尘灰比湿式水膜除尘灰脱硫效率高，并且电除尘的脱硫效率略微低于活性炭，同时介绍了粉煤灰的脱硫机理。     

城市给水厂给水污泥用于烧制粉煤灰-粘土砖的试验

城市给水厂产生的净水污泥(以下简称给水污泥),已成为治理城市固体废弃物污染的紧迫任务,以给水污泥为研究对象,进行了含水率60％-80％的给水污泥-粉煤灰-粘土烧制砖的成型、性能检测等试验研究。结果表明：在给水污泥-粉煤灰-粘土砖中掺人30％-45％(体积比)给水污泥,烧制成品符合国家标准(GB／T 5101-98)要求。     

Fly ash content and distribution in lake sediments around a large power station: inferences from magnetic susceptibility analysis

The bulk magnetic susceptibility of sediments from artificial and natural lakes around a large coal-fired power station in NE Spain has been measured. Higher magnetic susceptibility values are found in lake sediments located SE of the power station. This distribution of susceptibility values is compatible with environmental and meterological studies of emissions from the power station, which indicate a dominant SE plume direction. Mineralogical studies, by means of X-ray diffraction and scanning electron microscopy, show that the highest susceptibility values found in the sediments are caused by magnetic iron spinels in the fly ash that is transferred to the environment by the power station particulate emissions. After the quantitative mineralogical studies of fly ash, two different methods of fly ash content determination in the sediments have been devised, showing very similar results. The low background magnetic susceptibility of the sediments in the study area and the high susceptibility resulting from the input of magnetic fly ash particles allows both delimitation of the polluted area around the power station, and quantification of the fly ash input into the natural sediments.     

Dehalogenation Potential of Municipal Waste Incineration Fly Ash

BACKGROUND, AIMS AND SCOPE: In the first part of this paper the main principles which control the dehalogenation of polychlorinated aromatic compounds on municipal waste incineration fly ash (MWI-FA) have been discussed and the model fly ash of similar dehalogenation activity has been proposed. Even if both systems show comparable dehalogenation properties, the main question concerning the postulated identical reaction mechanism in both cases is left unanswered. The other very important point is to what extent is this dechlorination mechanism thermodynamically controlled. The same problem is often discussed in the literature also for the de novo synthetic reactions. From the data it is clear that metallic copper plays a decisive role in the mechanism of the dehalogenation reaction. Although the results reported in the first part strongly support the idea that copper acts in this dechlorination as the reaction component, in contrast to its generally accepted catalytic behaviour, we believed that additional support for this conclusion can be obtained with the help of a thermodynamic interpretation of the mechanism of the reaction. RESULTS AND DISCUSSION: The pathways of hexachlorobenzene dechlorination on MWI-FA and model fly ash were studied in a closed system at 260-300 degrees C under nitrogen atmosphere. These pathways were the same for both systems, with the following prevailing sequences: hexachlorobenzene --> pentachlorobenzene --> 1,2,3,5-tetrachlorobenzene --> 1,3,5-trichlorobenzene --> 1,3-dichlorobenzene. Thermodynamic calculations were carried out by using the method of minimization total Gibbs energy of the whole system. In the calculations, the following reaction components were taken into account: all gaseous chlorinated benzenes, benzene, hydrogen chloride, a gaseous trimer Cu3Cl3, and also Cu2O and CuCl2 as solid components. The effect of the reaction temperature and the amount of copper and water vapour were considered as well. The effect of reaction temperature was determined from the data calculated for the 500 to 750 K temperature region. The effect of the initial composition was determined for the molar amounts of copper = 0.01-3 moles and water vapour = 0.2 to 3 moles per mole of chlorobenzene isomer CONCLUSIONS: The results of hexachlorobenzene dechlorination by MWI-FA and model fly ash under comparable reaction conditions allow us to conclude that both dechlorinations proceed via the same dechlorination pathways, which can be taken as an evidence of the identical dehalogenation mechanism for both systems. The relative percentual distribution of the dehalogenated products depends on the temperature, but not on the initial amount of water vapour or copper metal. On the other hand, the initial amount of copper substantially affects the conversion of the dehalogenation as well as the molar ratio of Cu3Cl3 to HCl in the equilibrium mixture. Comparison of the experimental with thermodynamic results supports the idea that dehalogenation reactions are thermodynamically controlled. RECOMMENDATIONS AND OUTLOOK: Thermodynamic analysis of the dehalogenation reactions may prove useful for a wide range of pollutants. The calculations concerning polychlorinated biphenyls and phenols are under study.