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.     

A new approach for layout optimization in maintenance workshops with safety factors: The case of a gas transmission unit

In this study, an Integrated Simulation-Data Envelopment Analysis (DEA) approach is presented for optimum facility layout of maintenance workshop in a gas transmission unit. The process of repair of incoming parts includes various operations on different facilities. The layout problem in this system involves determining the optimum location of all maintenance shop facilities. Layout optimization plays a crucial role in this type of problems in terms of increasing the efficiency of main production line. Standard types of layouts including U, S, W, Z and straight lines are considered. First, the maintenance workshop is modeled with discrete-event-simulation. Time in system, average waiting time, average machine utilization, average availability of facilities, average queue length of facilities (AL) and average operator utilization are obtained from simulation as key performance indicators (KPIs) of DEA. Also, safety index and number of operators are considered as other KPIs. Finally, a unified non-radial Data Envelopment Analysis (DEA) is presented with respect to the stated KPIs to rank all layouts alternatives and to identify the best configuration. Principle Component Analysis (PCA) is used to validate and verify the results. Previous studies do not consider safety factor in layout design problems. This is the first study that presents an integrated approach for identification of optimum layout in a maintenance workshop of gas transmission unit by incorporating safety and conventional factors.     

Environmental risk mapping of accidental pollution and its zonal prevention in a city

Accidental releases of pollution can have severe environmental, societal, economic, and institutional consequences. This paper considers the use of risk mapping of accidental pollution events, and zonal prevention measures for alleviating the impact on large urban areas. An Environmental Pollution Accident Risk Mapping (EPARM) model is constructed according to a mapping index system supported by quantitative sub-models dedicated to evaluating the risk arising from different sources of potential accidental pollution. The EPARM approach consists of identifying suitable indexes, assessment of environmental risk at regional and national scales based on information on previous pollution accidents and the prevailing environmental and social conditions, and use of GIS to map the overall risk. A case study of pollution accidents in Minghang District, Shanghai, China is used to demonstrate the effectiveness of the model. The paper also proposes a systemic framework for accidental environmental pollution risk prevention, and detailed countermeasures for specific risk zones.     

基于交通冲突技术的交织区交通安全评价

为了分析城市快速路多个交织区之间的相对交通安全状况,及比选同一个交织区的多个设计方案,建立基于交通冲突技术的交织区交通安全评价方法。首先,使用微观交通仿真软件模拟一定道路交通条件下车流运行状态及其随时空变化的过程,并生成车辆轨迹文件;然后,运用交通安全替代评价模型(SSAM)分析车辆轨迹文件,识别和统计交通仿真过程中"发生"的交通冲突;最后,以交织区交通冲突数与交织区交通量、交织区长度的比值作为评价指标,评价交织区的交通安全状况。案例分析表明,交织区交通冲突率越高,其服务水平往往越低;交织区的交通冲突率有随交织区交通量增加而增加,随交织区长度、交织区车道数的增加而降低的趋势。     

反渗透技术在内陆核电站中的能量回收

核电站的用水安全是保障核电站安全运行的重要环节.根据内陆核电站补给水的水质要求及我国内陆地表水水质,提出了利用两级反渗透技术将水质较差的地表水经过处理作为内陆核电厂一、二回路循环冷却水补给水的工艺流程设计方案,并在两级RO过程中加入正位移式(液压往复式)能量回收器来达到降低能耗的目的.     

高层建筑火灾中安全疏散的评价分析

由于高层建筑的迅猛发展,高层建筑的火灾防范和安全疏散成为一个重要的研究课题。笔者阐述高层建筑的火灾特点,以及人员安全疏散的安全评价在消防中的重要作用;综述火灾危险分析的方法;介绍几种可以用于安全疏散的评价方法,并结合各种评价方法的优缺点进行了比较。根据实际情况,选择了模糊综合评价法对某一高层建筑作了简单的算例,从其结果中可以看出:疏散楼梯、防排烟和通风空调系统及事故疏散标志、通信设备存在一些问题,需要整改,以确保人员疏散的安全性;制定相应的应急预案,调整人员疏散策略,确保火灾中人员安全、及时、迅速撤离火灾现场,至安全区域。     

Bipolar charged aerosol agglomeration and collection by a two-zone agglomerator

ＩｎｔｒｏｄｕｃｔｉｏｎＢｅｃａｕｓｅｏｆｔｈｅｌｏｗｅｆｆｉｃｉｅｎｃｙｏｆｔｈｅｅｌｅｃｔｒｏｓｔａｔｉｃｐｒｅｃｉｐｉｔａｔｏｒ (ＥＳＰ)ｆｏｒｃｏｌｌｅｃｔｉｎｇｔｈｅｓｕｂｍｉｃｒｏｎｐａｒｔｉｃｌｅｓ ,ｔｈｅｅｌｅｃｔｒｉｃａｌａｇｇｌｏｍｅｒａｔｉｏｎｍｅｔｈｏｄｈａｓｌｅｄｔｏａｎｉｎｃｒｅａｓｉｎｇｉｎｔｅｒｅｓｔｉｎｒｅｄｕｃｉｎｇｔｈｅｅｍｉｓｓｉｏｎｏｆｔｈｅｆｉｎｅｐａｒｔｉｃｌｅｓ .Ｍａｎｙａｕｔｈｏｒｓｈａｖｅｓｔｕｄｉｅｄｅｌｅｃｔｒｉｃａｌａｇｇｌｏｍｅｒａｔｉ…     

介质阻挡放电联合催化臭氧化降解甲苯

采用介质阻挡放电区后结合MnOx/Al2O3/发泡镍去除甲苯,考察甲苯进气方式、臭氧产生方法及湿度对甲苯与O3同时去除的影响。结果表明,O3是等离子体区后催化降解甲苯的主要物种,介质阻挡放电联合催化臭氧化可实现甲苯及O3的同时高效去除。输入电压为9.0 kV时,甲苯的去除效率达92.8%,在80 min内O3的去除效率维持在99%以上。水蒸气对催化剂催化分解臭氧的活性没有直接的影响,O3浓度较高时湿度对甲苯降解效率的影响很小。GC-MS分析结果表明,甲苯降解的主要气相副产物有烷烃、酸、酮和含苯环有机物,提出了甲苯的降解途径。     

Determination and discussion hydraulic retention time in membrane bioreactor system

Based on the microorganism kinetic model, the formula for computing hydraulic retention time in a membrane bioreactor system (MBR) is derived. With considering HRT as an evaluation index a combinational approach was used to discuss factors which have an effect on MBR. As a result, the influencing factors were listed in order from strength to weakness as: maximum specific removal rate K, saturation constant Ks, maintenance coefficient m, maximum specific growth rate ,ua and observed yield coefficient Yobs. Moreover, the formula was simplified, whose parameters were experimentally determined in petrochemical wastewater treatment. The simplified formula is θ= 1.1( 1/β -1)(Kｓ S)/KXo , for oetroehemical wastewater treatment K and Ko eaualed 0.185 and 154.2, resoectively.     

Survey of polycyclic aromatic hydrocarbons (PAHs) in arterial street air of Hangzhou

ＩｎｔｒｏｄｕｃｔｉｏｎＰｏｌｙｃｙｃｌｉｃａｒｏｍａｔｉｃｈｙｄｒｏｃａｒｂｏｎｓ (ＰＡＨｓ)ａｒｅｗｉｄｅｓｐｒｅａｄｅｎｖｉｒｏｎｍｅｎｔａｌｐｏｌｌｕｔａｎｔｓｉｎｔｈｅａｔｍｏｓｐｈｅｒｅ.Ｔｈｅｙａｒｅｇｅｎｅｒａｔｅｄｉｎｔｈｅｃｏｍｂｕｓｔｉｏｎ .Ｔｈｅｍａｊｏｒｓｏｕｒｃｅｓｉｄｅｎｔｉｆｉｅｄｉｎｃｌｕｄｅｆｏｓｓｉｌｆｕｅｌｓ,ｖｅｈｉｃｕｌａｒｔｒａｆｆｉｃ,ｉｎｄｕｓｔｒｉａｌｐｒｏｃｅｓｓｅｓ,ｓｍｏｋｉｎｇａｎｄｄｏｍｅｓｔｉｃｈｅａｔｉｎｇ (Ｐｅｌｔｏｎｅｎ ,1995) .Ｔ…