浅谈加油站IC卡卡机联动改造工程中的HSE管理

介绍了HSE管理体系在加油站IC卡卡机联动改造工程中的应用 ,阐述了制定与实施HSE管理方案的重点 ,分析了IC卡改造工程中实施HSE管理的意义。     

Accounting for the effect of concentration fluctuations on toxic load for gaseous releases of carbon dioxide

In Great Britain, advice on land-use planning decisions in the vicinity of major hazard sites and pipelines is provided to Local Planning Authorities by the Health and Safety Executive (HSE), based on quantified risk assessments of the risks to the public in the event of an accidental release. For potential exposures to toxic substances, the hazard and risk is estimated by HSE on the basis of a “toxic load”. For carbon dioxide (CO₂), this is calculated from the time-integral of the gas concentration to the power eight. As a consequence of this highly non-linear dependence of the toxic load on the concentration, turbulent concentration fluctuations that occur naturally in jets or plumes of CO₂ may have a significant effect on the calculated hazard ranges. Most dispersion models used for QRA only provide estimates of the time- or ensemble-averaged concentrations. If only mean concentrations are used to calculate the toxic load, and the effects of concentration fluctuations are ignored, there is a danger that toxic loads and hence hazard ranges will be significantly under-estimated.This paper explores a simple and pragmatic modification to the calculation procedure for CO₂ toxic load calculations. It involves the assumption that the concentration fluctuates by a factor of two with a prescribed square-wave variation over time. To assess the validity of this methodology, two simple characteristic flows are analysed: the free jet and the dense plume (or gravity current). In the former case, an empirical model is used to show that the factor-of-two approach provides conservative estimates of the hazard range. In the latter case, a survey of the literature indicates that there is at present insufficient information to come to any definite conclusions.Recommendations are provided for future work to investigate the concentration fluctuation behaviour in dense CO₂ plumes. This includes further analysis of existing dense gas dispersion data, measurements of concentration fluctuations in ongoing large-scale CO₂ release experiments, and numerical simulations.     

Cost pass-through to higher ethanol blends at the pump: Evidence from Minnesota gas station data

We examine the pass-through of wholesale prices to retail prices in the market for E85, which contains 51%–83% ethanol, and in the much larger market for E10, which contains 10% ethanol. We use a panel dataset consisting of monthly observations from 2007 to March 2015 on wholesale and retail prices for 274 Minnesota gas stations that sell both E10 and E85. Consistent with prior research, the cumulative pass-through coefficient for E10 is 1.00 after one month. In contrast, the E85 market is sparse, and although pass-through increased over time, we estimate it to be only 0.53 statewide from 2012 to 2015. Pass-through is higher at stations with more local E85 competitors. In the Twin Cities, which has a high density of E85 stations, pass-through is nearly complete, but outside the Twin Cities slightly less than half the wholesale discount of E85, relative to E10, is passed on to the consumer.     

空气幕对城际铁路地下车站火灾烟气控制数值分析

为将空气幕作为城际铁路地下车站控烟措施提供理论依据,进而为地下车站防灾控烟设计提供新思路,以某典型城际铁路地下车站岛式站台层为依托,采用火灾动力学三维模拟软件FDS建立全尺寸火灾模型,对比单吹式、吹吸式空气幕布置于站台与轨行区间时楼梯及站台处温度及可见度分布规律,并分别对单吹式、吹吸式空气幕的射流风速、射流角度进行了参数优化研究。结果表明:单吹式、吹吸式空气幕均可保证火灾下楼梯区域可见度和温度的安全性要求;单吹式在射流风速为12 m/s且射流角度为10°时,吹吸式在射流风速为8 m/s时,防烟效果良好且趋于稳定;采用单吹式的最小站台危险区域较吹吸式长15 m,建议在城际铁路地下车站中选用吹吸式空气幕。     

Trace metal emissions from co-combustion of refuse derived and packaging derived fuels in a circulating fluidized bed boiler

Energy recovery from refuse derived fuels (RDF) and packaging derived fuels (PDF) is one option in integrated waste management. Nine RDF and PDF co-combustion tests with peat and coal in a circulating fluidized bed boiler were carried out in this work. Heavy metal emissions in flue gas and fly ash were measured. Multivariate data analyses were used to find out the most important parameters affecting metal emissions in the flue gas.

The results showed that total heavy metal emissions were low. Although RDF and PDF had more heavy metals than peat and coal, the multivariate data analysis showed that an increase of the RDF or PDF share in the fuel mixture up to 20% did not correlate directly with the metal emissions in the flue gas. Distribution of Cd, Cu, Zn and Sn between flue gas and fly ash correlated with each other. Injection of limestone to bind sulphur and chlorine did not have a significant effect on heavy metal emissions in the flue gas. Heavy metals concentrated on the fly ash, but all fly ashes passed the EPA-TCLP tests.     

Trimethylbenzoic acids as metabolite signatures in the biogeochemical evolution of an aquifer contaminated with jet fuel hydrocarbons

Evolution of trimethylbenzoic acids in the KC-135 aquifer at the former Wurtsmith Air Force Base (WAFB), Oscoda, MI was examined to determine the functionality of trimethylbenzoic acids as key metabolite signatures in the biogeochemical evolution of an aquifer contaminated with JP-4 fuel hydrocarbons. Changes in the composition of trimethylbenzoic acids and the distribution and concentration profiles exhibited by 2,4,6- and 2,3,5-trimethylbenzoic acids temporally and between multilevel wells reflect processes indicative of an actively evolving contaminant plume. The concentration levels of trimethylbenzoic acids were 3-10 orders higher than their tetramethylbenzene precursors, a condition attributed to slow metabolite turnover under sulfidogenic conditions. The observed degradation of tetramethylbenzenes into trimethylbenzoic acids obviates the use of these alkylbenzenes as non-labile tracers for other degradable aromatic hydrocarbons, but provides rare field evidence on the range of high molecular weight alkylbenzenes and isomeric assemblages amenable to anaerobic degradation in situ. The coupling of actual tetramethylbenzene loss with trimethylbenzoic acid production and the general decline in the concentrations of these compounds demonstrate the role of microbially mediated processes in the natural attenuation of hydrocarbons and may be a key indicator in the overall rate of hydrocarbon degradation and the biogeochemical evolution of the KC-135 aquifer.     

射流曝气的气液两相流的数值模拟

射流曝气在活性污泥处理方法中起着重要的作用。采用数值模拟的方法研究自吸式单级单喷射流器中的气液两相流动状况，通过对不同长径比和喷嘴面积比的射流曝气器模型的气液两相流的计算，定量分析长径比和喷嘴面积比对射流曝气器流场和空气与工作介质流量比的影响，为进一步设计开发新型高效的射流曝气器提供参考。     

Emissions from RDF/coal blended fuel combustion

The significant volume and weight reduction along with the energy potential of MSW, in the form of refuse derived fuel (RDF), has made its incineration an attractive alternative. However, the gaseous emissions such as, CO₂, CO, NO_x and SO₂, which are the byproduct of the combustion process pose serious environmental problems. These problems are compounded by the presence of certain highly regulated hazardous wastes such as, dioxins and furans in the exhaust stream. In the present investigation, different compositions of RDF/Coal blends were examined and the gaseous emissions from the combustion of the briquetted fuel were measured. Also, a direct comparison of emissions from RDF/coal blend incineration with coal combustion is presented in this paper. The potential for recovery of ferrous and non- ferrous metals provides an additional economic motivation for the use of RDF/Coal blended briquettes.     

包装废弃物添加脱氯半焦制备SRF的热解及动力学特性

利用热重红外分析仪(TG-FTIR)对包装废弃物添加了4种不同比例脱氯半焦制备而成的固体衍生燃料(SRF)的热解特性及热反应动力学进行了研究分析.研究发现,4种燃料热解过程主要包括4个阶段,其中300~400℃和400~500℃为两个主要失重阶段.前一阶段,SRF-1失重显著高于SRF-2、SRF-3和SRF-4,而后一阶段失重分别呈2、3、4倍增加.4种燃料热解残余量的顺序为SRF-4SRF-3SRF-2SRF-1,即添加了脱氯半焦的燃料热解程度越高.FTIR分析表明,添加了脱氯半焦的SRF燃料第三失重峰处不产生氯代烃.随脱氯半焦添加量的增加,第二失重峰CO2产生的浓度减少;第三失重峰CH4析出浓度增加;第四失重峰CO2析出的浓度增加.采用DEAM分布活化能法得到,转化率α0.3时,SRF-2和SRF-3的活化能均高于SRF-1的活化能,0.3α0.9时(α为0.6时除外),SRF-2、SRF-3和SRF-4 3种燃料的活化能低于SRF-1,且SRF-1的活化能呈升高的趋势,而其他3种燃料呈相反趋势.脱氯半焦的添加有利于SRF燃料的热解.