Wastewater-nitrogen removal using polylactic acid/starch as carbon source: Optimization of operating parameters using response surface methodology

The use of PLA/starch blends for nitrogen removal was achieved. The influence of different operating parameters on responses was verified using RSM. The conditions for desired responses were successfully optimized simultaneously. Blends material may have a promising application prospect in the future. Nitrogen removal from ammonium-containing wastewater was conducted using polylactic acid (PLA)/starch blends as carbon source and carrier for functional bacteria. The exclusive and interactive influences of operating parameters (i.e., temperature, pH, stirring rate, and PLA-to-starch ratio (PLA proportion)) on nitrification (Y₁), denitrification (Y₂), and COD release rates (Y₃) were investigated through response surface methodology. Experimental results indicated that nitrogen removal could be successfully achieved in the PLA/starch blends through simultaneous nitrification and denitrification. The carbon release rate of the blends was controllable. The sensitivity of Y₁, Y₂, and Y₃ to different operating parameters also differed. The sequence for each response was as follows: for Y₁, pH>stirring rate>PLA proportion>temperature; for Y₂, pH>PLA proportion>temperature>stirring rate; and for Y₃, stirring rate>pH>PLA proportion>temperature. In this study, the following optimum conditions were observed: temperature, 32.0°C; pH 7.7; stirring rate, 200.0 r·min^-1; and PLA proportion, 0.4. Under these conditions, Y₁, Y₂, and Y₃ were 134.0 μg-N·g-blend^-1·h^-1, 160.9 μg-N·g-blend^-1·h^-1, and 7.6 × 10³ μg-O·g-blend^-1·h^-1, respectively. These results suggested that the PLA/starch blends may be an ideal packing material for nitrogen removal.     

PSAT和BPA在电力系统潮流计算中的对比研究

针对当前电力系统分析程序存在差异的问题,从潮流计算角度,对比研究了国内目前使用较为普遍的2款潮流计算程序(PSAT和PSD-BPA),分析了收敛误差、发电机分接头、负荷比例等不同初值条件设置对其潮流计算结果的影响。分析结果表明:PSAT在建模、可视化和自定义方面具有一定优势,比较适合小规模电网仿真和自定义元件模型研究;而BPA的计算速度快,计算精度高,比较适合大规模电网仿真。     

一种PM_(2.5)辅助监测系统的设计与实现

为解决目前国内外PM2.5监测仪器价格昂贵,运行成本高,单点负责区域大,监测点少的问题,提出以国家监测网络为基础,以低成本、高精度为特点的PM2.5辅助监测方法。系统采用DSM501A作为PM2.5浓度采集传感器,完成粒子数量浓度到质量浓度的转换,通过在一定区域内布置监测终端,并借助于GPRS网络和参数曲面构建方法,建立了一定区域内PM2.5质量浓度网络图,填补了国家监测点间的监测盲区,并利用高斯消元法建立了从历史数据到未来浓度的预测算法。实验结果表明:实测数据与国家监测点数据基本一致,具有广阔的应用前景。     

电视、中波发射塔对电磁辐射环境的影响

通过对包头市城区历年的电磁环境监测,以及电视和中波发射塔周围电磁辐射情况,了解其环境质量状况和主要污染源。历年环境监测综合场强为0.30~0.47 V/m,年平均值为0.41 V/m。而广播和电视发射塔因距离而异,它们综合场强均值分别为1.26~3.43 V/m、1.44~5.34 V/m。虽然这些监测值都在标准限值之内,但可以看出广播和电视发射塔对电磁辐射综合场强的影响极大。     

钢铁行业废水零排放技术探索

针对钢铁行业废水特点,分析了目前钢铁行业各工序及全厂主要废水污染控制措施,重点分析了二级反渗透工艺的主要流程及进出水水质,以及该工艺存在的主要问题。通过对大型钢铁集团的现场调研,以太钢采用的反渗透和蒸发结晶工艺为例分析了钢铁行业真正实现废水零排放的技术可行性。该技术可以很好解决钢铁行业浓盐水的外排问题。     

BS EN ISO 20345：2011《个体防护装备安全鞋》标准的解析和建议

本文通过对最新的BS EN ISO 20345：2011《个体防护装备安全鞋》标准的列表介绍和概括性分析,找出了新标准检测项目仍存在的遗留问题和未考虑到的缺陷以及需要界定的术语,并提出了今后标准的再修订意见。此再修订意见的给出,为推动今后与安全鞋标准BS EN ISO 20345：2011属于同一体系的我国GB 21148-2007《个体防护装备安全鞋》标准修订提供参考意见。     

桂林中小河流洪涝气象风险预警系统设计

基于自动站、数值预报和雷达估测降水等多种雨量资料,利用ArcGIS技术提取河流的经纬度、流域范围,利用泰森多边形技术计算流域面雨量,结合对桂林中小河流域的历史暴雨洪涝风险个例分析结果,确定临界面雨量,建立桂林中小河流域洪涝灾害风险等级预警系统。利用数学内插技术进行雨量精细化插值,实现全市100多个水库、200多条河流关键点的雨量监测、预报、预警。利用Web和GIS技术实现桂林中小河流洪涝预警网页发布。     

双齿许水蚤(Pseudodiaptomus dubia)对亚热带虾池Cu和Zn富集的研究

重金属污染是对虾养殖环境主要污染现象之一,查明重金属在环境中的迁移规律对养殖水质调控和对虾健康养殖具有重要意义。本文采用火焰原子吸收分光光度计测定在不同暴露时间下双齿许水蚤(Pseudodiaptomus dubia) 对Cu和Zn的富集量,研究了双齿许水蚤对Cu和Zn富集动力学,并探讨了温度和盐度对其富集的影响。结果表明：双齿许水蚤对Cu和Zn的富集过程均经历了快速、慢速和平衡3个阶段,实验24 h达到富集平衡;双齿许水蚤对Cu和Zn的富集动力学参数k_1(Cu)=0.077 < k_1(Zn)=0.272,BCF_(Cu)=0.344 < BCF_(Zn)=2.252,双齿许水蚤对Zn的富集速率和富集能力均大于Cu。温度对双齿许水蚤Cu和Zn富集的影响显著(p <0.05),最适温度范围为15~30 ℃;盐度对双齿许水蚤Zn富集的影响极显著(p <0.01),而对Cu富集的影响不显著(p >0.05),对Cu和Zn适宜的富集盐度范围为5~35。这些研究结果表明,双齿许水蚤对Cu和Zn均具有较强的富集能力。基于以上研究结果,在对虾养殖期间,应通过循环过滤设施去除受到重金属污染池塘中的浮游动物,从而减少幼虾对其摄食和量度体重金属的积累,降低食品安全隐患。     

Removal of 17β-estradiol in laccase catalyzed treatment processes

The removal of 17β-estradiol （E2） in laccase catalyzed oxidative coupling processes was systematically studied in this work. We focused on the influence of pH and natural organic matter （NOM） on the performance of the enzymatic treatment processes. It was found that the optimal pH for E2 removal was between 4 and 6. The removal of E2 was slightly inhibited in the presence of NOM. Enzymatic transformation of E2 was second-order in kinetics with first-order to both the concentrations of the enzyme and contaminant. Mass spectrum （MS） analysis suggested that coupling products were formed through radical-radical coupling mechanism. The results of this study demonstrated that laccase catalyzed oxidative coupling process could potentially serve as a treatment strategy to control steroid estrogens.     

A red water occurrence in drinking water distribution systems caused by changes in water source in Beijing,China: mechanism analysis and control measures

A red water phenomenon occurred in several communities few days after the change of water source in Beijing, China in 2008. In this study, the origin of this problem, the mechanism of iron release and various control measures were investigated. The results indicated that a significant increase in sulphate concentration as a result of the new water source was the cause of the red water phenomenon. The mechanism of iron release was found that the high-concentration sulphate in the new water source disrupted the stable shell of scale on the inner pipe and led to the release of iron compounds. Experiments showed that the iron release rate in the new source water within pipe section was over 11-fold higher than that occurring within the local source water. The recovery of tap water quality lasted several months despite ameliora- tive measures being implemented, including adding phosphate, reducing the overall proportion of the new water source, elevating the pH and alkalinity, and utilizing free chlorine as a disinfectant instead of chloramine. Adding phosphate was more effective and more practical than the other measures. The iron release rate was decreased after the addition of 1.5 mg. L-1 orthophosphate- P, tripolyphosphate-P and hexametaphosphate-P by 68%, 83% and 87%, respectively. Elevating the pH and alkalinity also reduced the iron release rate by 50%. However, the iron release rate did not decreased after replacing chloramine by 0.5-0.8 mg. L-1 of free chlorine as disinfectant.