钻井井喷失控因素分析及预防对策

井喷失控是钻井中的灾难性事故,有必要开展井喷失控研究,找到井喷失控发生的原因和提出防止井喷失控的对策。在统计分析1970年到2009年间中石油发生在钻进过程中的48例井喷失控事故的基础上,通过对防喷器、节流压井管汇、套管、井喷后爆炸起火等井喷失控因素分析,并利用MLS法对上述各种井喷失控因素危险值进行评估。最后,根据井喷失控因素分析和危险值评估结果,结合现有的钻井井控设计,提出了防止钻井井喷失控的对策。     

矿井通风网络复杂度与风机控制力量化计算

为了探究矿井通风网络复杂度与风机控制力的关系,提出分支关联度、最小距离、通风网络复杂度和风机控制力的概念。利用vCad2.0进行数字实验,对网络复杂度与风机控制力的关系进行定量研究。结果表明:随着网络复杂度的增加,矿井通风系统的有效风量率减小,且认为该值减小到60%时,视为风机控制力的极限,此时网络拓扑结构为风机所能控制的最大网络复杂度。地面集中供风时,同时工作的中段数量存在上限,最大值为7。将结论用于某有色金属矿进行实证研究,找出该矿深部中段通风困难的原因,为矿井进一步整改提供理论依据。     

急冷器建造中的质量保证

本文以百万吨乙烯装置的关键设备裂解气急冷器建造为例,从设计视角对其建造过程中重要环节质量控制进行剖析,详细解读了压力容器建造质量保证体系运行的基本要务。压力容器建造质量保证的关键在于合理制定并严格执行符合设计标准规范要求的质量计划,尤其是建造过程各环节的工艺卡制定与控制点的检查确认要深入到位。如此得出：压力容器建造质量计划的执行既是压力容器质量保证体系有效运行的见证,更是以建造过程控制达到不产生不合格进而实现压力容器本质安全的根本保证。     

变换炉的风险评估技术

在设计阶段对压力容器出具风险评估报告会增加设计难度,也对设计人员有了更高的要求。针对如何具体实施风险评估,本文提出了煤化工行业变换炉的风险评估的技术,以便与同行交流,旨在推广风险评估技术,促进风险评估技术的应用推广。     

珠江三角洲机动车排放控制措施协同效应分析

预测了2015年珠江三角洲机动车空气污染物和温室气体排放量,设计了6类单一控制、技术控制、结构控制以及综合控制措施的情景,并运用基准线年排放清单编制和协同效应坐标系法分析了污染物与温室气体减排的协同效应.结果表明,按目前机动车保有量增长趋势,2015年污染物和温室气体将以18%~120%的幅度增加;各控制措施下污染物和温室气体排放量均有下降,且均具有正向的协同效应,但减排的贡献差异较大.6类单一控制措施中淘汰黄标车和结构性控制措施分别对各污染物和温室气体的削减效果最明显,减排幅度均在40%以上,且正向协同效应突出,但相比其他措施,结构性控制措施实施难度大.     

日本琵琶湖污染源系统控制及其对我国湖泊治理的启示

琵琶湖富营养化全面有效的控制得益于对流域污染源的系统控制. 琵琶湖流域污染源系统控制包括通过立法与监管严格控制工厂与企业的污水排放、城镇污水管网与大型污水处理设施的高度覆盖、农业集落污水处理设施的全覆盖三部分,流域污水处理系统的全覆盖及高度处理技术的普及是其最为成功的经验之一. 琵琶湖流域城镇下水道普及率达86.4%,主要污染物——TN、TP及COD_Mn的去除率分别高达90.0%、98.7%及94.6%. 琵琶湖流域同时实施了净化槽普及、设置农业集落排水处理设施、初期雨水净化处理及农田循环灌溉等具有地方特色的面源治理对策. 通过综合治理,琵琶湖主要入湖污染负荷明显减少,与1985年相比,2012年COD_Mn点源污染负荷减少了76.8%,TN减少了45.5%,TP减少了65.6%. 与之比较,我国的湖泊治理存在的问题主要包括有针对性的地方排放标准的缺失及执法力度的不足、城镇污水深度处理及运营管理技术上的差距、面源污染对策的严重不足.      

Determination of polychlorinated biphenyl and polycyclic aromatic hydrocarbon marine regional Sediment Quality Guidelines within the European Water Framework Directive

Marine regional Sediment Quality Guidelines (SQG) for polychlorinated biphenyls (PCB) and polycyclic aromatic hydrocarbons (PAH) from the Basque coast (SE Bay of Biscay) were determined, on the basis of sediment chemistry, toxicity and benthic community disturbance from analysis of 756 estuarine and coastal samples. The SQG were calculated using a percentile approach (based upon effect and non-effect data), using non-normalised and normalised concentration, by total organic carbon. However, normalisation by total organic carbon did not result in any improvement in accuracy compared with non-normalised values. Hence, this study proposes non-normalised SQG values for assessment of the chemical and physicochemical status in marine waters in the Basque Country, within the Water Framework Directive: 24.6–29 μg kg^?1 for total PCBs; 164–285 μg kg^?1 for low molecular weight PAH; 922–1537 μg kg^?1 for high molecular weight PAH; and 1607–2617 μg kg^?1 for total PAH.     

Villains,victims, and heroes: Accounting for the roles human activity plays in LOPA scenarios

When a team is analyzing a LOPA scenario, the team needs to consider all three roles played by human interaction in the scenario: that of cause, as a result of human error; that of receptor, both in terms of safety impacts (inside the fence line) and community impacts (outside the fence line); and that of independent layer of protection (IPL), considering both administrative controls and human responses. Frequently, the nature of these three roles are inter-related, and setting guidance that is internally consistent is important to using LOPA to assess risk rather than as a means to game the analyses to simply achieve a wished-for result.A number of criteria have been proposed to quantify human involvement, typically as cause, as receptor, or as IPL. Establishing a framework to look at all three in a unified way is more likely to result in analyses that are consistent from scenario to scenario.This paper describes such a framework and presents it in a way that allows organizations to review their own criteria for quantifying human involvement in LOPA. It also examines some of the published LOPA criteria for human involvement and looks at them in terms of consistency of approach between evaluation of cause, receptor, and IPL. Finally the paper makes suggestions to use in calibrating LOPA methodologies to achieve consistent and believable results in terms of human interaction within and between scenarios that have worked for other organizations.     

A/O脱氮工艺实时控制对策的试验研究

以人工合成废水为研究对象,系统研究了提高A/O(anoxic/oxic)工艺氨氮和硝酸氮去除效率的实时控制对策.氨氮控制的本质是通过控制DO设定值和好氧区体积大小使出水氨氮浓度达标排放.硝酸氮控制的本质在于高效利用缺氧区反硝化潜力,为此建立了以调节内循环回流量或(和)外碳源投加量维持缺氧区末端硝酸氮浓度处于设定值的实时控制对策.系统控制采用两级结构,高水平监控层用来选择低水平执行层的设定值,而低水平执行层对DO值、好氧区体积、内循环回流量和外碳源投加量进行直接控制,试验表明上述控制对策可以显著提高系统脱氮效率,降低出水氨氮和硝酸氮浓度,并最大程度节约运行费用.     

机房安全监控系统软件浅析

计算机机房的安全监控软件可分为本地监控软件和远程监控软件两大类,分别就目前这两类软件的特点及其发展趋势做了比较和分析,为用户选择安全监控软件提供了参考和建议。