Vent burst pressure effects on vented gas explosion reduced pressure

The overpressure generated in a 10 L cylindrical vented vessel with an L/D of 2.8 was investigated, with end ignition opposite the vent, as a function of the vent static burst pressure, P_stat, from 35 to 450 mb. Three different K_v (V^2/3/A_v) of 3.6, 7.2 and 21.7 were investigated for 10% methane–air and 7.5% ethylene–air. It was shown that the dynamic burst pressure, P_burst, was higher than P_stat with a proportionality constant of 1.37. For 10% methane–air P_burst was the controlling peak pressure for K <∼8. This was contrary to the assumption that P_red > P_burst in the literature and in EU and US standards. For higher K_v the overpressure due to flow through the vent, P_fv, was the dominant overpressure and the static burst pressure was not additive to the external overpressure. Literature on the influence of P_stat at low K_v was shown to support the present finding and it is recommended that the influence of P_stat in gas venting standards is revised.     

The explosion parameters of methanol under variable pressures and 423 K

The high-temperature and high-pressure methanol one-step oxidation has been the primary process for the mass production of dimethoxymethane. However, the risk of explosion for this process is still not properly defined. This paper presents new results from the experimental study on the explosion characteristics, including the explosion pressure and the explosion limits for methanol/air mixtures with a variable oxygen level, under an initial pressure between 0.3 MPa and 0.75 MPa and at the initial temperature of 423 K. The upper explosive limits were found to increase along with the initial pressure. If the limits for normal air are known, the oxygen effect on flammability is predictable from the thermal balance method. With a correlation for the pressure effect and a method for the oxygen effect, we can have the flammable range predictable.     

Industrial accidents in spray dryer plants for dairy products in Europe

Despite the fact that the information about past accidents is an integral part of accident prevention, the information about industrial accidents is not commonly available in food and agricultural sectors. Spray dryer plants for dairy products are not an exception. The aim of this paper is the creation of the representative database for industrial spray drying accidents in order to identify their major causes. The paper is divided into 8 chapters. The first two chapters deal with the general information about technology of spray drying of dairy products. The third chapter provides the outputs from the authors' database containing records of 25 accidents in milk drying facilities in Europe. These accidents took place between 1999 and 2019 in six European countries. Based on the accident database, the most common causes of accidents were identified. Processes that can cause a fire, an explosion, or damage to environment are described in the fourth, fifth and sixth chapter. The seventh chapter deals with process, technical and organizational measures; these were discussed using literature research and the results of the accident database. The eighth chapter is the conclusion with a focus on further improvement of process safety through newly developed protective tools.     

面粉增白剂生产过程中发生爆炸的主要原因及防范措施

分析了面粉增白剂主要成份过氧化苯甲酰（ＢＰＯ）在生产过程中发生爆炸的主要原因，对生产、检修、储存等诸环节中可能发生爆炸的危害程度进行了比较，从设施、设备、工艺流程、工具、仪表、制度、人员素质等方面提出了防止爆炸的可行措施     

Public Discourse and the Rhetorical Construction of the Technospecter

Modern technological disasters and their human and environmental consequences often defy the imagination in their immensity and complexity. As such, their rhetorical constructions often lack tangibility and a sense of material reality for those not directly involved. These amorphous constructions are consolidated into a view of technological disaster and threats of disaster in which the rhetorical dimensions are analogous to those of ghosts portrayed in popular literature and film—a view the author terms the “technospecter.” Drawing on the public discourse surrounding a tragic pipeline explosion near Carlsbad, New Mexico, this study identifies the rhetorical dimensions of the technospecter and discusses how the construction of the specter reinforces the meta-narratives that constrain pro-environmental action.     

一起焦硫酸贮罐爆炸的技术分析

某焊工在对一焦硫酸贮罐施焊时 ,发生了爆炸事故 ,本文对这一事故进行了分析 ,并提出了预防措施。     

Coal dust particle size survey of US mines

The National Institute for Occupational Safety and Health (NIOSH) and the Mine Safety and Health Administration (MSHA) conducted a joint survey to determine the range of coal particle sizes found in dust samples collected from intake airways of US coal mines. The last comprehensive survey of this type was performed in the 1920s. The size of the coal dust is relevant to the amount of rock dust required to inert the coal dust, with more rock dust needed to inert finer sizes of coal dust.

Dust samples were collected by MSHA inspectors from several mines in each of MSHA's 10 bituminous Coal Mine Safety and Health Districts. Samples were normally collected in several intakes at each mine. The laboratory analysis procedures included acid leaching of the sample to remove the limestone rock dust, sonic sieving to determine the dust size, and low-temperature ashing of the sieved fractions to correct for any remaining incombustible matter. The results indicate that particle sizes of mine coal dust in intake airways are finer than those measured in the 1920s. This finer size coal dust in intake airways would require more incombustible matter to be effectively inerted than the 65% incombustible specified in current regulations.     

Modeling of BP Texas City refinery incident

This paper presents detailed modeling results of the BP Texas City refinery incident. Three different approaches and explosion modeling tools were used to study the event. The results predicted by all three approaches are similar and all approaches identified a hazard potential comparable to what was witnessed on March 23, 2005. This confirms that quantitative risk assessment (QRA) has the ability to model a realistic scenario, and is therefore useful in safety measure design and emergency preparedness decision making to improve overall safety performance. Had QRA been conducted during a management of change (MOC) decision-making process, personnel trailers likely would not have been sited in such close proximity to the process units. The resulting severe consequences would then not have occurred. This work also aims to emphasize the importance of QRA in process safety management.

The paper presents the authors’ perception of the sequence of events involved in the incident based on the published literature available at the time of writing. It also assesses potential consequences for the perceived sequence of events using a variety of consequence assessment tools. In doing so, the analysis illustrates how this incident could have been prevented in spite of many operational difficulties. The observations and commentary presented in this paper are intended solely for the purpose of process safety enhancement on the basis of the lessons learned. BP has published its own detailed report; the incident is also the subject of a recent investigation by the US Chemical Safety and Hazard Investigation Board, with the CSB's final report being available at http://www.csb.gov/index.cfm?folder=completed_investigations&page=info&INV_ID=52 (as of April 2007).     

Effect of scale on flame speeds of methane-air

Explosions are the main types of accidents causing casualties in underground coal mines. Research on the mechanisms of gas explosions is needed as a basis for the development of techniques and strategies for explosion prevention, suppression, and mitigation. The prevention of loss in explosion accidents and inquiries into their causes require understanding of the explosion process of methane in air. Because of the high cost and safety issues in full scale experiments, the experiments with small scale ducts have become a key alternative approach. Whether the experimental results at small scales agree with those at full scales needs to be investigated to validate the significance of the experimental results at small scale. Numerical simulation was used to obtain the explosion characteristics of a methane-air mixture in a gallery or duct. If the grid size is too fine in the numerical simulation for a methane-air explosion it is difficult to calculate using the present computer resource. If the grid size is too coarse, the considerable error may result. The effect of grid size on results of calculation depends on the scenario being investigated. The effect of grid sizes on simulation accuracy was analyzed in this work. The overpressure and temperature distributions and the flame propagation for the deflagration of methane-air mixtures in a gallery or duct were obtained by the AutoReaGas code at three different scales. The geometry of investigated objects and the grids in the calculation domain were similar in the three cases. The calculated overpressures vary with the scale. The calculated temperatures do not vary with the scale for the three cases.     

Investigations on explosion characteristics of ethyl acetate

In this study, the confined explosion characteristics of ethyl acetate were investigated in a constant volume explosion vessel using the initial pressure of 1–4 bar, the initial temperature of 358–418 K, and the equivalence ratio of 0.8–1.4. It was revealed that the peak explosion pressure and the maximum pressure rise rate of ethyl acetate increased as the initial pressure increased and the initial temperature decreased. The peak explosion pressure and maximum pressure rise rate were obtained at the equivalence ratio of 1.2 due to increased heat release rate. Furthermore, the explosion time decreased as the initial pressure decreased. In summation, EA experimental and theoretical deflagration index were investigated and compared. The experimental deflagration index showed that EA explosion was less dangerous, whereas the theoretical deflagration predicted that the explosion could be more hazardous.