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     

旋流分离技术在污水处理中的应用

介绍旋流分离器在含油污水处理应用中的工作原理、基本结构、功能及特点。旋液分离罐的基本结构及在生产应用中的改造、运行情况。     

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。     

质点群动态分布律及其应用

质点群动态分布律,可定量地表示进入容器或空间内的质点群,受外力作用后,当其产生沉降或运动时的状态分布特征,并简介用它来解决重力、离心力、静电力、磁力及其合力作用下的一系列各类除尘器或分选器的基本理论问题和部分工程实际方面的问题.     

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.