强化混凝去除黄浦江水有机物的试验研究

强化混凝去除有机物的效果与水源的分子量分布特性有着密切的关系.由于黄浦江水中低分子量的溶解性有机物占多数,因此,强化混凝处理有机物效果有限.对于＜1k分子量区间的有机物.增加混凝剂投量可有效去除紫外吸光值(UV254),但去除溶解性有机碳(DOC)的效果很差.尽管增加混凝剂投量和降低pH都能有效地去除有机物,但决定强化混凝效果的主要因素是pH,去除黄浦江水有机物的最佳pH范围为6～5.     

1000MW机组电除尘器的设计及技术改进

介绍了1000MW机组电除尘工程的特点及其电除尘器的设计难点,针对1000MW机组电除尘器设计中的诸多不利因素提出了具体的改进措施。     

中波发射台电磁辐射环境影响理论预测与模拟类比方法的比较分析

中波台发射设备项目电磁辐射环境影响评价采用理论计算和模拟类比方法结果一致,运用理论计算方法评价结果相对偏安全。     

强化混凝工艺深度处理给水厂排泥废水

水厂废水的综合处理与回用是我国供水行业的新趋势和节水目标所在,采用强化混凝技术进行水厂排泥废水的深度处理。通过混凝剂筛选实验和有机物表征确定最佳混凝剂为高效聚合铝(HPAC),适宜投加量为650 mg/L。当混凝剂HPAC投加量为650 mg/L时,对COD、TOC、浊度和色度的去除率分别为82.5%、89.8%、95%和92.5%,相应的出水值分别为58 mg/L、8.46 mg/L、2.35 NTU、13度,COD满足《污水综合排放标准》(GB 8978-1996)的要求(COD≤100 mg/L),同时实验结果显示聚合氯化铝(PAC)、HPAC、三氯化铁(FeCl3)主要去除分子量处于>1 300 Da范围的有机物,对分子量处于744～1 300 Da之间的有机物去除有限。     

某电厂600MW火电机组脱硫增容改造方案探讨

按照国家环保部文件要求,大唐集团河北某电厂600 MW机组湿法脱硫系统需进行增容改造。该电厂根据实际情况,归纳了3种可行的脱硫增容改造方案,即原吸收塔增加喷淋层和高度、双吸收塔串联、双吸收塔双循环,阐述了各自的技术特点,结合性能保证、工程投资、施工周期等影响因素,比较了各方案的优缺点。经过对比和论证,双吸收塔方案比单吸收塔方案更适合于本次工程改造。     

Purification and molecular weight distribution of a key exopolysaccharide component of Bacillus megaterium TF10

Extracellular polymeric substances (EPS) are organic metabolic compounds excreted by microorganisms. They largely impact microbial aggregate structures and functions. Extracellular polysaccharides (EP) in EPS are responsible for the formation of microbial aggregates. In this work, we successfully separated and characterized EP from EPS of the bacterium Bacillus megaterium TF10. Extraction of EP from EPS was optimized using Sevag''s reagent. Chemical characteristics, functional groups, and molecular weight (MW) distribu-tion of EP were compared with the harvested EPS and soluble microbial products (SMP). We found that the polymers of lower MW and free proteins were successfully removed by Sevag''s reagent. The higher MW components of EPS were predominantly polysaccharides, while the polymers of lower MW tended to secrete to the supernatant and were described as SMP. A part of the proteins in the EP was polysaccharide-bonded. Our results can be further used in elucidating the complex flocculation mechanisms in which EP play a major role.     

330MW循环流化床机组协调控制系统的特点分析与应用实例

循环流化床机组在动态特征上不同于煤粉炉,其燃料煤粒较粗,燃烧过程复杂,并且因为其燃烧室内的床料具有相当大的热惯性和蓄热能力,是以当给煤量改变后,主蒸汽压力的变化相应比煤粉锅炉的迟延和惯性要大得多,造成了循环流化床机组燃烧过程实现自动协调控制的困难。以京海煤矸石发电有限责任公司凤凰岭电厂新建工程2×330 MW循环流化床机组控制系统为例,从变参数的应用、前馈的应用、主压力与给水的解耦控制、煤质修正控制等多方面阐述了循环流化床机组的控制特点,分析探讨了应用中存在的问题并提出了解决方法。     

Optimization of the recovery of plastics for recycling by density media separation cyclones

Material recovery processes are presented as the optimum option for recycling plastic wastes as a means of recovering hydrocarbon resources. There exist a large variety of automated material recovery processes for recycling of such wastes but each with significant limitations. Of these, the separation based on differences in densities is advocated as the optimum process either for producing recycled products or preparing wastes for subsequent recovery processing.Density separation processes based on cyclone type density media separation (DMS) is presented as an important, potential method for increasing plastics recycling process capacities. It is demonstrated to have the capacity to separate a significantly larger range of particle sizes than those presently processed industrially. The mathematical relationship for the prediction of quality of typical LARCODEMS type density media separations by particle size and density as expressed by the Ecart Probable is presented.A proposed device configuration is presented for density media separation to optimize the recovery and purity of both density fractions produced. It is also suggested that to be economically viable, a large scale of operation is required for industrial plastics recycling operations recovering and producing a number of different plastics with a purity to be used as a substitute for virgin material.     

Fouling of nanofiltration membrane by e uent organic matter: Characterization using di erent organic fractions in wastewater

The UF membrane with molecular weight cuto (MWCO) ranging from 2 to 100 kDa and XAD-8 resin were employed to identify the characteristic of molecular weight (MW) distribution of wastewater e uent organic matter (EfOM) in terms of TOC and UV254, as well as the amounts of the hydrophilic/hydrophobic organic fractions in di erent MW ranges. Then, the nanofiltration (NF) membrane fouling experiments were carried out using the above fractionated water to investigate the e ect of MW distribution and hydrophilic/hydrophobic characteristics of EfOM on the membrane flux decline using the fractionated water samples. The experimental results have shown that 45.61% of the total organics belongs to the low MW one, among which the percentage of the hydrophilic organics with low MW (less than 2 kDa) was up to 28.07%, while that of the hydrophobic organics was 17.54%. In particular, the hydrophilic fraction was found to be the most abundant fraction in the e uents. MW distribution has a significant e ect on the membrane fouling. When the MWwas less than 30 kDa, the lower the MW, the larger was the specific flux decline, while in the case of MW higher than 30 kDa, the higher the MW, the larger was the specific flux decline, and the decline degree of low MW organics was larger than the high MW one. With the same MW distribution range, specific flux decline of the hydrophilic organic was considerably slower than that of the hydrophobic organic, which indicated that the hydrophobic organic fractions dominantly contribute to the flux decline.     

太湖原水中膜污染物质的确定与表征

采用混凝沉淀和浸没式微滤膜联用技术处理太湖原水,考察组合工艺中的有机物亲疏水性和分子量分布变化,并分析化学清洗水的有机物组分,以期确定造成膜污染的主要物质成分.结果表明,混凝预处理可有效去除大分子的亲水性有机物,这类有机物仅能导致可逆污染,而中等和小分子的有机物会导致不可逆污染.此外,三维荧光光谱表明与膜污染关系最密切的2个区域为:λex=230nm/λem=330~350nm (区域Ⅰ)和λex=280nm/λem=300~350nm (区域Ⅳ),其对应的胞外蛋白质类有机物和溶解性微生物产物(SMP)是造成微滤膜不可逆污染的主要物质.