曝气生物滤池处理农村污水的中试研究

采用研制的曝气生物滤池对农村污水进行处理,研究其性能特点和影响因素。结果表明：在气水比为5∶1,水力停留时间（HRT）为15 h,进水COD浓度在250 mg/L以下时,COD和氨氮的去除率分别在80％和90％以上,出水COD和氨氮值达到国家《城镇污水处理厂污染物排放标准》一级A标准;反应器在冬季水温12℃以上运行时出水COD和氨氮值比在夏季运行时有所上升,但去除率仍在80%和90%以上,可以达到排放标准。     

A model for radiological consequences of nuclear power plant operational atmospheric releases

A dynamic dose and risk assessment model is developed to estimate radiological consequences of atmospheric emissions from nuclear power plants. Internal exposure via inhalation and ingestion, external exposure from clouds and radioactivity deposited on the ground are included in the model. The model allows to simulate interregional moves of people and multi-location food supply in the computational domain. Any long-range atmospheric dispersion model which yields radionuclide concentrations in air and on the ground at predetermined time intervals can easily be integrated into the model. The software developed is validated against radionuclide concentrations measured in different environmental media and dose values estimated after the Chernobyl accident. Results obtained using the model compare well with dose estimates and activities measured in foodstuffs and feedstuffs.     

从全混流反应器热稳定性的角度探讨高危工艺的危险性

通过对全混流反应器(CSTR)热平衡条件下多态的分析,探讨热稳定性条件,并对一级不可逆反应在CSTR中的热稳定性进行定性分析;探讨不同反应热和活化能对反应过程热稳定性的影响,及其对反应器发生"飞温"事故要求紧急停车时的控制要求的影响,进而从反应工程的角度对高危工艺的界定提出新的思路。分析结果表明,工艺的危险性不仅与工艺的种类相关,更与工艺本身的热力学、动力学特征密切相关。通过对高危工艺的热稳定状况的分析,能够动态地揭示其在温度扰动下发生"飞温"或"熄火"的过程,从本质上把握高危工艺潜在的危险性,并能有针对性地制定自动化改造方案,提高化工企业的本质安全度。     

粒子阻隔效率测试仪串行通信数据处理系统

在GB2626—2006《呼吸防护用品——自吸过滤式防颗粒物呼吸器》中防尘面罩粒子阻隔效率测定是一项评价防尘面罩性能的关键指标。为实现数据通信及处理的自动化操作,提高检测效率,本研究针对装置的串行数据通信的底层接口,开发基于EXCELVB脚本的串行通信数据处理系统。该系统为更好地研究实粒子阻隔效率测定方法和阻隔效率相关规律提供了便利条件。     

硝酸盐氮,亚硝酸盐氮总量紫外吸收快速测定

水体中尤其是海水中硝酸盐氮的测定较繁琐,干扰物质多,分析时间长,重现性差,准确性不高。文章通过实验介绍一种省时、省力、简便可行不消耗化学试剂且抗氯化物干扰、精度和准确度较高的硝酸盐氮、亚硝酸盐氮总量测定方法。     

生物泥浆反应器中微生物数量变化与PAHs降解

分别以浓度、温度、接种量、通气量和表面活性剂为降解调控因子,采用平板记数法进行了生物泥浆反应器中微生物数量变化与ＰＡＨｓ降解的关系研究。结果表明：土壤中细菌数量与ＰＨＥ、ＰＹ投加浓度呈显著正相关。ＰＨＥ、ＰＹ初始浓度越高,细菌数量越大。此外,反应器的温度对微生物生长速度和数量有重要影响。反应器温度为３０℃时对细菌迅速繁殖有利,反应器温度为２０℃时对真菌生长繁殖有利。接种量为５％即可明显提高ＰＨＥ和     

Grey Box and Component Models to Forecast Ozone Episodes: A Comparison Study

For the purpose of short-term forecasting of high ozone concentration episodes stochastic models have been suggested and developed in the literature. The present paper compares the quality of forecasts produced by a grey box and a component time-series model. The summer ozone patterns for three European urban areas (two continental and one mediterranean) are processed. By means of forecast performance indices according to EC and WHO guidelines, the following features of the models could be found: The grey box model is highly adaptive and produces forecasts with low error variance that increases with the time horizon of forecast. The component model is more 'stiff' that results in a higher forecast-error variance and poorer adaption in detail. The forecast horizon, however, could be enlarged with this model. The accuracy of predicting threshold exceedance is similar for both models. This can be understood from the assumption of a cyclical time development of ozone that was made for both models.     

烟尘滤筒称重方法的改进

针对在烟尘测试中滤筒的称重存在天平显示不稳、恒重难的现象进行了探讨。比较了2种称量方法,提出在平衡室中冷却、称量滤筒,并采用标准滤筒来减小由于称重条件不同而产生的系统误差。结果表明,改进方法具有称量稳定、易恒重、失重少的优势。     

Treatment of tannery wastewater by electrocoagulation

Treatment of tannery wastewater by electrocoagulation with low cell current(≤1A)and soluble electrodes(mild steel electrodes and aluminum electrodes)was studied.Compared with aluminum electrodes,mild steel electrodes were more effective for the removal of sulfide,with a removal efficiency of over 90%.But during the treatment process,black color precipitate typical to iron(Ⅱ)sulfides was produced.While aluminum electrodes were effective to eliminate the colority of the effluent,the removal efficiency of sulfide was lower than 12%.The mechanisms of the removal of chemical oxygen demand,ammonia,total organic carbon,sulfide and colority with the two soluble electrodes(mild steel and aluminum electrodes)were discussed in detail.In order to exert the predominance of diffenent types of electrodes,the tannery wastewater was treated using mild steel electrodes first followed by the filter and finally by the aluminum electrodes,the elimination rates of chemical oxygen demand,ammonia,total organic carbon,sulfide and colority were 68.0%,43.1%,55.1%,96.7% and 84.3%,respectively,with the initial concentrations 2413.1 mg/L,223.4 mg/L,1000.4 mg/L,112.3 mg/L and 256 dilution times,respectively.The absorbance spectra and energy consumption during electrocoagulation process were also discussed.     

Effect of cycle time on biodegradation of azo dye in sequencing batch reactor

The effects of cycle time on the biodegradation of the azo dye remazol brilliant violet 5R (RBV-5R) were investigated in an anaerobic–aerobic sequencing batch reactor (SBR). System performance was determined by monitoring chemical oxygen demand (COD), color, anaerobic enzyme (azo reductase) and aerobic enzyme (catechol 2,3-dioxygenase), and aromatic amine concentration. SBR was operated in three different total cycle times (48 h, 24 h and 12 h), fed with a synthetic textile wastewater. In this study, the anaerobic period of SBR was found to allow the reductive decolorization of azo dye and the aerobic period was found to be effective on further COD removal after the anaerobic period. The percentage reductions in color by the anaerobic stage of the SBR were at 72%, 89% and 86% for the 24-h, 12-h and 6-h cycle times, respectively. Total COD removal efficiencies were over 75% for all operational conditions and about 70% of the COD removal was achieved in the first 3 h of anaerobic stages. During the decolorization of RBV-5R, two sulfonated aromatic amines (benzene-based and naphthalene-based) were formed and detected by HPLC. Aerobic phases of SBR with total cycle times of 48 h, 24 h and 12 h were able to remove benzene-based aromatic amines with removal efficiency of 64%, 92% and 89%, respectively. The results indicated that the best SBR performance in terms of color removal and aromatic amine degradation was achieved from total cycle time of 24 h.