条斑紫菜养殖对海区中无机氮浓度影响

2002年10月至2003年4月期间对江苏吕泗条斑紫菜栽培海区海水的无机氮进行跟踪监测。结果表明紫菜栽培可以降低整个海区的无机氮含量。在三种无机氮中,硝酸氮和亚硝酸氮的浓度变化不如氨氮明显,说明紫菜优先利用氨氮。     

模糊综合评价在天然水体水质评价中的应用研究

采用模糊数学方法,对河网地区面源污染影响较大的代表性河流的水质状况进行综合评价研究。根据监测断面水质污染特点,确定了8个指标作为评价因子,建立了评价因素矩阵,计算出影响因子的权重。在此基础上,提出了模糊综合评价的水质级别,证明该河网地区的污染物主要是氮、磷和有机物。     

光纤ZnO薄膜的制备及光催化性能研究

实验利用射频磁控溅射镀膜工艺,分别在光纤和石英玻璃上成功制备了ZnO薄膜。采用X射线衍射仪、原子力显微镜和荧光分光光度计对薄膜进行了测试分析,并对其光催化降解苯酚的性能进行了对比测试。结果表明,该薄膜具有良好的C轴取向性,光致发光峰分别位于362nm、421nm和486nm附近,且随着薄膜样品晶粒的减小而出现蓝移,光纤上ZnO薄膜的光催化能力是以石英玻璃为基底的ZnO薄膜的193倍,光催化效果显著。     

有机磷农药生物降解技术研究进展

有机磷农药是目前国内外使用较多的化学农药,对人、畜均有毒性。长期以来,人们努力寻找降解有机磷农药的方法,以去除其对人类生活的不利影响。对现有的有机磷农药种类、毒性、生物降解技术以及现有成果进行了系统的归纳和总结,并对有机磷农药生物降解的进一步研究提出了建议。     

臭氧在中试规模污泥原位减量中的应用

为探究高、低浓度臭氧旁路处理对中试系统出水水质、污泥减量率的影响,采用两组系统(对照组:厌氧/缺氧/好氧(A/A/O),试验组:A/A/O+臭氧旁路处理)在5个工况下运行183d.结果表明,利用剂量为13mg/g MLSS(25mg/g MLVSS)臭氧处理占生物反应池容积20％的回流污泥时,系统运行性能良好;在此操作...     

基于FLAC3D分析的某铁矿充填效果研究

为解决辽宁某铁矿开采后地表沉陷问题,验证自研的复合激发尾砂胶结充填体充填效果,运用FLAC3D模拟软件对铁矿二步骤充填开采和地表沉陷进行数值模拟计算研究.研究结果表明:采用3种胶结充填体分别进行二步骤充填后,盐基、碱基、水泥基胶结充填体内部的应力平均值分别为0.92,0.79,0.93 MPa,最大位移值分别为38,2...     

Denitrification and phosphorus uptake by DPAOs using nitrite as an electron acceptor by step-feed strategies

Denitrifying phosphorus accumulating organisms (DPAOs) using nitrite as an electron acceptor can reduce more energy. However, nitrite has been reported to have an inhibition on denitrifying phosphorus removal. In this study, the step-feed strategy was proposed to achieve low nitrite concentration, which can avoid or relieve nitrite inhibition. The results showed that denitrification rate, phosphorus uptake rate and the ratio of the phosphorus uptaken to nitrite denitrified (anoxic P/N ratio) increased when the nitrite concentration was 15 mg·L^-1 after step-feeding nitrite. The maximum denitrification rate and phosphorus uptake rate was 12.73 mg NO2-–N·g MLSS-1?h-1 and 18.75 mg PO43-–P·g MLSS-1?h-1, respectively. These rates were higher than that using nitrate (15 mg·L^-1) as an electron acceptor. The maximum anoxic P/N ratio was 1.55 mg PO43--P?mg NO2--N-1. When the nitrite concentration increased from 15 to 20 mg NO2--N?L-1 after addition of nitrite, the anoxic phosphorus uptake was inhibited by 64.85%, and the denitrification by DPAOs was inhibited by 61.25%. Denitrification rate by DPAOs decreased gradually when nitrite (about 20 mg·L^-1) was added in the step-feed SBR. These results indicated that the step-feed strategy can be used to achieve denitrifying phosphorus removal using nitrite as an electron acceptor, and nitrite concentration should be maintained at low level (<15 mg·L^-1 in this study).     

城区天然气配气站噪声的产生及防治

城区天然气配气站噪声超标已成为供气部门亟待解决的难题,文章分析了配气站噪声污染现状,指出噪声产生原因主要为天然气流动,供气量增长使设备超负荷运行等7个方面。分别针对现有配气站和新建、改扩建站场提出降噪措施,指出设备在额定范围内运行、气体流速控制、工艺改造等是噪声控制的重要手段。并对城区天然气配气站噪声治理的进一步研究提出了建议。     

机柜振动、冲击响应特性的试验研究

机柜是设备的安装架,当其受到某一安装平台的振动与冲击作用后,随着安装位置的不同,机柜内安装的单元设备所经受的振动、冲击量值和谱型也有很大不同。因此对于单元设备的振动、冲击考核条件不应等同于整系统的要求,而应该根据其安装平台的响应制定。     

Mathematical modelling of sewage sludge incineration in a bubbling fluidised bed with special consideration for thermally-thick fuel particles

Fluidised bed combustor (FBC) is one of the key technologies for sewage sludge incineration. In this paper, a mathematical model is developed for the simulation of a large-scale sewage sludge incineration plant. The model assumes the bed consisting of a fast-gas phase, an emulsion phase and a fuel particle phase with specific consideration for thermally-thick fuel particles. The model further improves over previous works by taking into account throughflow inside the bubbles as well as the floating and random movement of the fuel particles inside the bed. Validation against both previous lab-scale experiments and operational data of a large-scale industrial plant was made. Calculation results indicate that combustion split between the bed and the freeboard can range from 60/40 to 90/10 depending on the fuel particle distribution across the bed height under the specific conditions. The bed performance is heavily affected by the variation in sludge moisture level. The response time to variation in feeding rate is different for different parameters, from 6min for outlet H(2)O, 10min for O(2), to 34min for bed temperature.