粉煤灰深度处理低浓度的磷

为了探讨低浓度磷吸附的方法,比较了粉煤灰、煤质活性炭和粉煤灰碎砖块颗粒这3种价廉易得的吸附材料的除磷效果。经对比确定以粉煤灰为吸附剂,研究了反应时间、粉煤灰投加量以及溶液p H对深度除磷效果的影响。同时为了解粉煤灰高效除磷原理,利用SEM和XRD对其表面形状、所含元素及其内部结构进行了表征。结果表明,粉煤灰比煤质活性碳和粉煤灰砖砖块颗粒的除磷效果更好,去除率高达98.9%;SEM和XRD表征结果显示,由于粉煤灰表面积较大、表面能高、含有Si—O—Si和Si—O—Al—O偶极键及铝、铁和钙的氧化物,使得粉煤灰对低浓度的磷有着高效的去除率;吸附磷后的粉煤灰表面形成了一层絮状物,经EDS分析显示其组成以钙磷沉淀为主;1 g粉煤灰对1 mg/L的磷酸盐溶液在p H=10、反应时间60 min时表现出最佳吸附性能。     

Chemical Behaviour of Calcium in Stabilized Oil Ash Reef Blocks After Five Years in the Ocean

Reef blocks made from stabilized oil ash were taken from the sea after five years in the ocean to examine the chemical behaviour of calcium. Experiments included (1) determination of the calcium leaching rate and a comparison with the rate for unexposed blocks to test the validity of a diffusion model for predicting long term (5 years) leaching rates, (2) determination of the effect of biological cover (shell) on the leaching rate, (3) determination of the leaching rate of the core of exposed reef blocks, (4) determination of the calcium content in 'ring areas' - regions of discoloration observed in sectioned exposed reef blocks, and (5) determination of the leachable fraction of the total calcium in exposed reef blocks. Results showed the presence of a pronounced calcium discontinuity zone located 3-7 cm from the outside surface of the reef blocks. Cumulated calcium release rates ranged from 2.81-3.14 μmol cm^-2 day^-1 for original unexposed reef blocks and the core of exposed (in the ocean for five years) blocks, respectively, to 0.47-0.50 μmol cm^-2 day^-1 for outside (facing sea water) surfaces of exposed reef blocks. Tank leaching studies also showed that the presence or absence of hard biological cover (shells) had little or no effect on the calcium release rate. the diffusion model normally used in modelling the chemical behaviour of calcium cannot be used to predict the long term (five years) leaching of calcium. the core of the exposed blocks released calcium at a rate similar to new, unexposed reef block material. Overall, it appears that the calcium discontinuity zone is probably responsible for restricting the release of calcium and hence the failure of the diffusion model.     

镁砂窑的黑烟治理

本文介绍了乡镇镁砂工业的主干装备———镁砂窑轻烧镁砂由燃煤改燃煤气的新工艺、煤的气化原理及反应顺序、镁砂窑改变燃料的比较计算、简易煤气发生炉的构造和煤气燃烧用的空气量计算等，并对镁砂窑采用煤气燃烧工艺后所产生的综合效果，作了简单的评价     

洁净型煤技术及推广应用探讨

洁净型煤的推广使用是有效控制煤烟型污染的一种重要手段，采用在原煤中添加化学药剂，重新加工成型的方法，达到降尘、固硫、节能的目的。通过推广使用，有效的降低二氧化硫、烟尘的产生量和排放量，减少对城市大气环境的污染，达到煤的热量高效、清洁利用。     

城市固体废弃物堆肥工艺条件试验研究

利用城市污水厂污泥、生活垃圾及粉煤灰进行堆肥试验研究 ,通过对 4组配比试验结果分析 ,合适的污泥、垃圾和粉煤灰堆肥配合比为 4∶5∶1,并对试验结果进行了讨论     

应用油团聚技术洁净烟煤的主要影响因素研究(一)

介绍了油团聚(SGHFF)技术脱除烟煤灰分的过程。经过四步浮选后,灰分的去除率可达到86.8％;探讨了影响油团聚技术过程的主要因素,为洗煤厂及煤矿的细煤泥的处理及解决环境问题提供有效途经。     

屋顶电除尘器湿式清灰探讨

根据屋顶电除尘器二次烟尘的特点，针对其清灰不彻底的问题，通过工程实践经验，设计了一种可动喷水清灰装置，在实践中应用良好，值得借鉴     

CO2对飞灰稳定化效果的影响

用CO2作为化学稳定剂或辅助稳定剂处理三种不同的来自实际垃圾焚烧厂的飞灰，并对处理后的飞样进行浸滤实验来衡量稳定效果。结果表明二氧化碳对飞灰中所含的重金属Pb和Cd具有稳定效果，对飞灰中的Cr有促进溶出的效果。当以磷酸盐和绿矾为稳定剂稳定飞灰中的重金属时，先采用CO2进行预处理基本不影响对Pb和Cd的稳定效果，但对Cr的浸出控制有明显的促进效果。     

燃煤锅炉烟气脱硫除尘一体化系统的无垢运行研究

在燃煤锅炉上采用双碱法脱硫工艺,分析了系统运行过程中可能出现的结垢问题,并进一步讨论了解决问题的方法。实验结果表明,将一定量进水投入浆池后,用石灰再生并补充纯碱后打入出水能有效防止系统内部的结垢,当进水的pH值为6.6￣6.8,浆池中水的pH值为10￣11时,系统无垢运行效果最佳。     

Use of zeolitized coal fly ash in the simultaneous removal of ammonium and phosphate from aqueous solution

Discharge of wastewater containing nitrogen and phosphate can cause eutrophication. Therefore, the development of an efficient material for the immobilization of the nutrients is important. In this study, a low calcium fly ash and high calcium fly ash were converted into zeolite using the hydrothermal method. The removal of ammonium and phosphate that coexist in aqueous solution by the synthesized zeolites were studied. The results showed that zeolitized fly ash could efficiently eliminate ammonium and phosphate at the same time. Saturation of zeolite with Ca²⁺ rather than Na⁺ favored the removal of both ammonium and phosphate because the cation exchange reaction by the NH₄ ⁺ resulted in the release of Ca²⁺ into the solution and precipitation of Ca²⁺ with PO₄ ³⁻ followed. An increase in the temperature elevated the immobilization of phosphate whereas it abated the removal of ammonium. Nearly 60% removal efficiency for ammonium was achieved in the neutral pH range from 5.5 to 10.5, while the increase or decrease in pH out of the neutral range lowered the adsorption. In contrast, the removal of phosphate approached 100% at a pH lower than 5.0 or higher than 9.0, and less phosphate was immobilized at neutral pH. However, there was still a narrow pH range from 9.0 to 10.5 favoring the removal of both ammonium and phosphate. It was concluded that the removal of ammonium was caused by cation exchange; the contribution of NH₃ volatilization to immobilization at alkaline conditions (up to pH level of 11.4) was limited. With respect to phosphate immobilization, the mechanism was mainly the formation of precipitate as Ca₃(PO₄)₂ within the basic pH range or as FePO₄ and AlPO₄ within acidic pH range.