动态水流条件下河流底泥污染物(COD_(Cr))释放研究

为了研究不同水深、流速等水动力条件对底泥中污染物释放强度的影响,以苏州河底泥为例,通过水槽试验,分析了动态水流条件下河流底泥中污染物释放及其对上覆水体水质的影响.结果表明,CODCr释放率随时间的增大而增大,但CODCr释放强度随时间的增大而减小.底泥中污染物释放率与水深和流速有关,在相同水深的条件下,底泥的释放率随着流速的增加而增大;在相同流速的条件下,底泥的释放率随着水深的增大而减小.在水深10cm、流速0.10m.s-1的动态水流条件下,底泥向上覆水体释放CODCr的释放强度与时间的关系为:C=1.06C0e-0.06t.     

区域水环境质量静态水量评价方法初步探讨

分析了现有的区域地表水环境质量综合评价方法的不足,提出了水环境质量与水资源量相结合的静态水量评价新方法,即根据各个监测断面水质和该断面所代表的水资源量,以某类别水质的各监测断面代表的水资源量之和占评价区域各类断面代表的水资源的总量百分比来表征评价区域整体水质状况。应用结果表明,本方法科学、合理、可行。     

伊春河河水水溶性腐殖酸内源释放模型

以水溶性腐殖酸含量很高的伊春河为例，利用冬季冰封无外源输入的条件，在有产室内模拟研究的基础上，通过现场采样及测定，建立了伊春河河水水溶性腐殖酸的内源释放模型，根据同期采集样品进行的验证表明，该模型能够准确地反映河流沉积物中水溶性瘁殖酸向河水中释放的速率以及速率与流速等条件的定量关系。     

湖泊沉积物中磷化氢的释放动力学初探

采用柱状芯样模拟法,研究了太湖沉积物-水界面磷化氢的释放动力学.结果表明:当沉积物-水界面磷化氢的释放达到动态平衡时,水界面中磷化氢的浓度基本不再增大,大约在0.34 pg·l-1左右,此时磷化氢的释放通量约为0.008 pg·dm-2·h-1.根据室内模拟结果,太湖沉积物每年的磷化氢释放量在13.81-49.62 g之间,从而使磷化氢在湖水中的平均浓度达到0.16 pmol·l-1.     

垃圾场渗出污水厌氧处理的可行性研究

采用血清瓶静态试验法研究了垃圾渗出污水的厌氧处理的可行性。试验表明:垃圾渗出污水对厌氧发酵微生物无抑制作用,有良好的厌氧降解性,产气率为0.321/g·COD,污水中的大部份有机物都能被厌氧消化,COD_cr去除率为78.2%,发酵过程中还能获得能源——沼气。具有良好的应用前景。     

Worst-case identification of gas dispersion for gas detector mapping using dispersion modeling

To quickly and accurately quantify the material release in process units, gas detectors may be placed according to the results of gas dispersion modeling. DNV's PHAST software is one of the most useful and reliable tools for material dispersion modeling. In this software, fluid dispersion is modeled based on the process conditions, the weather conditions and the specifications of the material release point. However, varying weather conditions throughout the year and the exact determination of the release point on the plot plan and the release elevation are problematic; these issues cause the results to be non-exact and non-integrated. Choosing the most appropriate conditions is challenging. In this paper, a scheme was provided to select the most appropriate conditions for gas dispersion modeling. This scheme approaches modeling based on the worst-case scenario (the situation in which the dispersed gas reaches the detector later in comparison to the other cases). Therefore, different weather conditions, release elevations and release points on the plot plan were modeled for an absorber tower of the Gonbadli Dehydration Unit of the Khangiran Refinery. The worst case of each release condition was then chosen. Finally, gas detectors were placed using the gas dispersion modeling results based on the worst-case scenario.     

Sea water quality monitoring in Rhodes and Cos (Greece)

During the years 1983–1986, a program aiming at monitoring water quality of the most crowded beaches, as well as assessing and minimizing pollution from certain land based sources was carried out in Rhodes and Cos. The program was directed towards inspections of treatment plants as well as laboratory analyses of treated effluents from large hotels. As a result, almost one in four hotels was obliged to construct a new treatment plant. In order to help personnel to improve plant efficiency through day‐to‐day maintenance a three day seminar was held in June 1985. Sea water quality parameters (total coliforms and E. coli) were found to be well below the limits set by E.E.C. directives.     

Polychlorinated dibenzo p-dioxins and dibenzofurans emissions in a primary copper smelter in China

Metallurgical production is the largest polychlorinated dibenzo-p-dioxins and dibenzofurans (PCDD/F) emission source in China. However, PCDD/F monitoring and research are rarely conducted on primary metallurgical production. In this study, a demonstration primary copper smelter in China was selected to investigate PCDD/F characteristics and control. Samples were collected from major PCDD/F release points in the smelter process (fly ashes and waste water sludge). Specific analysis of PCDD/F congeners was carried out using a high resolution gas chromatography/high resolution mass spectrometry method. The results showed that PCDD/Fs might be unintentionally produced in the primary copper smelter processes, with sample concentrations of 180–6110 pg/g dry wt; highly chlorinated PCDD/F homologues were predominant. The toxicity of all the samples was calculated to be 120 pg WHO TEQ/g, fly ashes from the refining process furnaces air pollution control device and sludge were hazardous waste with higher PCDD/F toxicity. Both precursor formation and de novo synthesis were found to contribute to PCDD/F formation in the smelter process. PCDD/F characteristics and formation were compared with reported secondary copper smelters. Life-cycle control of PCDD/F was proposed for retrofitting of this smelter and for similar plants in China's primary copper production sector, including control at the PCDD/F formation, removal and disposal stages.     

新型复合式除尘器

针对电、布除尘器的特点,提出了一种新型静电布袋混合式除尘器,并已应用于工业中。在没有使用任意阀门的前提下,该产品将电除尘器和布袋除尘器结合在一起,取长补短,充分发挥了电除尘器能大量收尘、节能、维护检修工作量小,还可捕集高比电阻和低比电阻等特殊干性粉尘,解决了电除尘难以净化的含微米或亚微米烟尘的难题。兼具布袋除尘器对粉尘粒度和比电阻不敏感、排放浓度低的优点。一级静电除尘器效率可达90%,对于粉尘浓度为30 g/m3左右的燃煤锅炉,经过静电除尘后进入滤袋的粉尘浓度只有3 g/m3。对于这种粉尘浓度,滤袋的清灰周期可达3 h以上。由于清灰周期的大大增长,可大大提高滤袋的寿命。该产品性价比优良、占地面积少、结构简单。尤其在净化效率、气体阻力等主要技术指标方面达到了环保要求。     

Experimental analysis of radiographer exposure to the static field from a 1.5-T magnetic resonance imaging machine

Introduction. This study measures the exposure of occupational therapists from a 1.5-T magnetic resonance imaging (MRI) machine. Method. A total of 14 time-series on each of the chest, head and hand were taken before and after different MRI procedures. The peak values were noted in each case together with an average of all data recorded in the time-series. Results. The highest exposure recorded was observed on the hand, followed by the head and the chest. The overall maximum exposure (1479.40?mT) recorded was observed on the hand during a change of coil. It was also observed that the recorded exposure of experienced radiographers working in the MRI environment was less than that of junior staff due to different practices. Conclusion. This study is of significant importance in Malta since it is the first conducted in a MRI environment, especially because the results were compared with limits imposed by EU Directive 2013/35/EU which has to be implemented by July 2016.