湿式除尘器的应用研究

新疆油田公司供热公司为提高除尘效率,减少SO_2排放量,将多管除尘器改造为湿式除尘器,介绍了湿式除尘器的结构和除尘原理。针对存在的问题,通过改进溢流箱结构解决了水位控制问题,烟气含尘量和SO_2排放量均达到GB 13271—2001《锅炉大气污染物排放标准》。介绍了利用纯碱、电石渣、锅炉的冲渣水与除尘器流出的冲灰水混合这三种烟气脱硫方法,其中,锅炉的冲渣水与除尘器流出的冲灰水混合的烟气脱硫方法综合效果最好。     

1000MW机组灰斗积灰输灰不畅原因分析及应对措施

介绍了国内百万超临界机组电除尘器灰斗积灰以及浓相气力输送系统输灰管道不畅的原因。针对其较严重的故障给出了具体详尽的解决方案,并给出了如何来避免此类故障发生的各种应对措施,以及在监视巡检中应掌握的措施,为百万火力发电机组的运行实践提供参考。     

不同改性剂改善污泥土工性质的比较研究

选择了泥土、矿化垃圾、粉煤灰和建筑垃圾4种改性剂改性城市污水处理厂污泥(以下简称污泥)。结果表明:(1)随着4种改性剂与污泥的混合比增大,混合物含水率降低。(2)当混合比为0.7(质量比)时,各种混合物的抗压强度都达到50kPa的填埋要求;当混合比为0.3～1.0时,混合物的抗压强度随着混合比的增大呈指数形式增大;比较4种改性剂对抗压强度的增大能力,粉煤灰最强,建筑垃圾次之,泥土和矿化垃圾较弱。(3)在50kPa预压力下,混合物要达到不小于25kPa的抗剪强度,泥土与污泥最小混合比为1.0,矿化垃圾与污泥最小混合比为1.0,粉煤灰与污泥最小混合比为0.7,建筑垃圾与污泥最小混合比为0.7。(4)除加泥土的混合物外,混合物压缩系数随着混合比的增大呈总体下降趋势。(5)粉煤灰除臭效果最好,矿化垃圾次之,建筑垃圾较差,泥土最差。     

红阳煤田红菱煤矿煤矸石地球化学特征及古环境恢复

通过对红菱煤矿7煤和12煤的顶板、底板和夹层煤矸石的矿物、常量、微量、稀土元素的分析发现,这三个层位的煤矸石有较大的区别。利用考奇法恢复古盐度,7煤显示淡水和咸水沉积,12煤有明显的咸水沉积特征。利用微量元素和稀土元素对物源性质及其构造背景分析,结果表明煤矸石的物质来源和构造背景较复杂,源区为长英质或基性岩石区,源区构造背景为大洋岛弧或被动大陆区。     

燃煤飞灰颗粒物中元素分布规律的研究

利用ICP-AES光谱仪和TOC总碳分析仪对不同粒级下的飞灰颗粒进行了元素测定,对元素分布规律的形成原因进行了分析.分析结果表明:煤经旋流燃烧器燃烧而未经过除尘设备的飞灰中300目以下小颗粒含量较高.随着燃烧温度的升高,大颗粒的含碳量增加,小颗粒的含碳量减少,元素Al、Mg、Cr在各个粒级中含量变化不大,Ti、Ba、V在大于280目的小颗粒中含量有下降趋势,其他大部分痕量元素在大于300目的小颗粒中得到富集.     

Alkaline hydrothermal conversion of fly ash precipitates into zeolites 3: the removal of mercury and lead ions from wastewater

In this paper, the utilisation of zeolites synthesised from fly ash (FA) and related co-disposal filtrates as low-cost adsorbent material were investigated. When raw FA and co-disposal filtrates were subjected to alkaline hydrothermal zeolite synthesis, the zeolites faujasite, sodalite and zeolite A were formed. The synthesised zeolites were explored to establish its ability to remove lead and mercury ions from aqueous solution in batch experiments, to which various dosages of the synthesised zeolites were added. The test results indicated that when increasing synthesised zeolite dosages of 5-20 g/L were added to the acid mine drainage (AMD) wastewater, the concentrations of lead and mercury in the wastewater were reduced accordingly. The lead concentrations were reduced from 3.23 to 0.38 and 0.17 microg/kg, respectively, at an average pH of 4.5, after the addition of raw FA zeolite and co-disposal filtrate zeolite to the AMD wastewater. On the other hand, the mercury concentration was reduced from 0.47 to 0.17 microg/kg at pH=4.5 when increasing amounts of co-disposal filtrate zeolite were added to the wastewater. The experimental results had shown that the zeolites synthesised from the co-disposal filtrates were effective in reducing the lead and mercury concentrations in the AMD wastewater by 95% and 30%, respectively.     

A novel approach to preparing ultra-lightweight ceramsite with a large amount of fly ash

•Ultra-lightweight ceramsite is prepared with 80% fly ash. •SiO₂, Al₂O₃, and flux contents significantly influence the performance of ceramsite. •The expansion of ceramsite is caused by the formation of a dense glaze and gas. •The bulk density of ultra-lightweight ceramsite is only 340 kg/m³. The disposal of fly ash has become a serious problem in China due to its rapid increase in volume in recent years. The most common method of fly ash disposal is solidification-stabilization-landfill, and the most common reuse is low-value-added building materials. A novel processing method for preparing ultra-lightweight ceramsite with fly ash was developed. The results show that the optimal parameters for preparation of ultra-lightweight ceramsite are as follows: mass ratio of fly ash:kaolin:diatomite= 80:15:5, preheating temperature of 800°C, preheating time of 5 min, sintering temperature of 1220°C, and sintering time of 10 min. The expansion agent is perlite, at 10 wt.% addition. Finally, a ceramsite with bulk density of 340 kg/m³, particle density of 0.68 g/cm³, and cylinder compressive strength of 1.02 MPa was obtained. Because of its low density and high porosity, ultra-lightweight ceramsite has excellent thermal insulation performance, and its strength is generally low, so it is usually used in the production of thermal insulation concrete and its products. The formation of a liquid-phase component on the surface, and generation of a gas phase inside ceramsite during the sintering process, make it possible to control the production of the suitable liquid phase and gas in this system, resulting in an optimization of the expansion behavior and microstructure of ceramsite. These characteristics show the feasibility of industrial applications of fly ash for the production of ultra-lightweight ceramsite, which could not only produce economic benefits, but also conserve land resources and protect the environment.     

MSWI BA treated with Advanced Dry Recovery: a field scale study on materials’ leaching properties

In many European countries, the environmental properties of waste-derived aggregates are mostly assessed based on laboratory leaching tests such as the standardised percolation tests CEN/TS/14405, ISO/TS 21268-3, or DIN 19528. These tests are conducted under specified conditions, which are similar yet somewhat different from realistic field conditions. Therefore, this study aimed to investigate the leaching properties of ADR (Advanced Dry Recovery) recovered MSWI BA in the field in order to understand more about its environmental impacts in actual civil engineering structures. Two field scale studies (a lysimeter and a larger interim storage field study) were constructed and the leachate quality was investigated. These results were then complemented with the results of previously conducted laboratory leaching tests using a liquid to solid ratio (L kg^?1) comparison. The results demonstrated that the leaching behaviours of many potentially harmful substances, such as chloride, copper and antimony, was similar despite the study scale. In addition, this study illustrated the importance of investigating the leaching properties of waste-derived aggregates on a larger scale, even though the uncertainties in such studies may not be easily controlled.     

Recovery of copper from small grain size fractions of municipal solid waste incineration bottom ash by means of density separation

Small grain size fractions of municipal solid waste incineration (MSWI) bottom ash (BA) contain elemental and chemically bonded metals in appreciable amounts, especially copper. Investigations with a centrifugal concentrator were carried out using samples, which had been treated with different impact devices. Partly the impacts of single devices were visible in outlines, but mostly the surfaces of the metals were still covered with mineral residues. To generate copper rich fractions, parameters of the separation process should ensure mass yields <2%, best between 0.5 and 1%. The density of the concentrates is then generally >3.2 g/cm³. Best results were achieved with material from a special treatment train which is adapted to grain sizes <2 mm. Reliable copper contents between 20 and 40% (single runs >50%) could be realised. However, considering the required mass yields, referred to this subset only 150–170 g copper would be recovered from 1 Mg MSWI BA. Furthermore, this copper is only in parts present in elemental form. A dependable added value of such treatment step seems to be given only, if that enables a recycling of the mineral aggregates (tailings) in parallel to avoid landfill costs.     

萃取法从粉煤灰生产Al_2O_3废水中回收偏硅酸钠

采用由C_1~C_4低碳醇组成的复配萃取剂萃取回收粉煤灰生产Al_2O_3废水(脱硅液)中的偏硅酸钠,在提取产品偏硅酸钠的同时回收脱硅液中的碱。直接进行萃取时偏硅酸钠易流失,萃取剂用量大,回收成本较高。将脱硅液浓缩后再进行萃取,萃取剂用量大幅减少,回收成本明显下降。将萃取剂成本与浓缩所需成本之和最低时的最佳浓缩比下、脱硅液与萃取剂体积比为1∶0.8时回收的偏硅酸钠干燥处理,干燥后的偏硅酸钠中Na_2O含量(w)大于20.5%,SiO_2含量大于20.0%,水不溶物含量小于0.05%,铁含量小于0.05%,白度大于70%,产品符合HG/T2568—2008《工业偏硅酸钠》标准。