指出在液化石油气爆炸事故类型中，泄漏型火灾爆炸发生的概率最大，也最危险。
It is pointed out that the probability of leakage type fire and explosion of LPG is highest, which is the most dangerous in all of the explosion accidents of LPG.
研究显示：将泡沫铝应用到油气类爆炸防护中是可行的，能有效衰减油气爆炸产生的冲击波。
The research shows it is feasible that aluminum foam is applied in fuel-air explosion and it can attenuate shock waves generated by fuel-air explosions effectively.
如果工作区域的油气浓度比最低爆炸浓度高出5%，必须使用呼吸器。
You must use a respirator if the fuel-gas concentration in the work area is 5% more than the lower explosive limit (LEL).
介绍了油罐清洗作业中存在的油气中毒、火灾爆炸和罐体变形等安全问题，并针对问题提出了解决办法。
The suitable time to clean oil tank and the safety problems such as oil gas poisoning, fire-explosion and tank deformation during cleaning operation are introduced.
结合现场分析了雷击爆炸的原因是雷电流沿油气管线进洞，在洞内放电跳火。
The reason for cave shorage explosion caused by lightning is the sparks brought about by the electric current that comes into the cave along oil and gas pipe-lines.
采用火灾爆炸危险指数评价法，对液化石油气储罐区火灾爆炸事故的危险性进行定量安全评价。
The fire and explosion hazard in liquefied petroleum gas storage tank zone were evaluated quantitatively by the fire and explosion hazard index method.
汽油是一种燃料，其油气容易爆炸。
在一定程度上，随着泡沫铝厚度、油气浓度（即爆炸荷载大小）的增加，降低板中心点处位移峰值的幅度也随之增加。
The decrease gradient of the peak displacement at the center of plate increases as the foam thickness, fuel-air concentration(i. e. explosion load size) increases to some extent.
结合液化石油气的典型案例，对液化石油气火灾爆炸事故发生的过程、机理和评价模型进行了研究与分析。
Research and analyses on the process, mechanism and assessment model for fire explosion accidents are conducted in accordance with several typical cases.
液化石油气的生产、储运过程中蒸气爆炸事故屡有发生，并导致其他类型的爆炸。
LPG vapor cloud explosions often occur in the production and transportation process and sometimes they cause other types of explosions.
火灾爆炸事件中约有10％属于静电事故，尤其在液化石油气站、油库、加油站等多次发生与静电有关的爆炸事故。
The accident of static electricity occupies 10 % of fire and explosion ones, especially, in LPG station, oil store and gas station ect.
油罐的火灾爆炸主要由点火源和油气泄漏造成。
Fire resources and leak of oil and gas result in fire and explosion in oil tank.
运用规范评价和危险程度评价相结合的方法，对液化石油气储配站发生火灾爆炸的危险性进行了定量安全评价。
Quantitative safety assessment on probability of fire and explosion in LPG storage and filling station is done by method of code evaluation combined with risk grade evaluation.
液化石油气蒸气爆炸是其储运过程中较易发生且危害极大的一种热力过程。
Vapor explosion of LPG happen frenquently during its storage and transportation, and the consequent damages are usually large.
油气储运系统是石油工业的大动脉，另一方面又可能是火源、爆炸源和污染源。
Oil gas storage and transport systems are big arteries of the petroleum industry, while they may also be the causes of fire, explosion and pollution.
液化石油气储罐在火灾作用下，其内部的温度和压力迅速上升，从而会引起储罐爆炸，进而酿成危害性更大的二次灾害。
When LPG tanks are exposed to external fire, their temperature and pressure will increase rapidly, which may cause the tanks exploding and lead the secondary hazard with much more damage.
液化石油气(LPG)在其运输和存储过程中存在着各种与火灾和爆炸相关的危险性。
The liquefied petroleum gas (LPG) has multifarious risks associated with fire or explosion in the traffic and storage process.
对液化石油气储运过程中的各种爆炸类型及成因进行了探讨，运用事故树方法分析了引起火灾爆炸的概率和原因。
A systematical analysis on LPG explosion type and cause during storage and transportation of LPG is made. A Failure Tree Method is used to find the explosion probability and cause.
建立了绝热稳态爆炸泄压计算模型，对不同泄压口位置情况下油气混合物爆炸泄压过程中压力、温度等参数进行了计算。
Established is a calculation model of isolation and stable state explosive pressure relief and calculated are such parameters as pressure and temperature during explosive pressure relief.
上周在维亚雷乔火车站附近，一辆货运列车出轨，导致两节载有液化石油气的油罐车爆炸，造成附近两座建筑物倒塌。
A freight train derailed and two liquefied petroleum gas-filled tankers exploded near the Viareggio train station, causing two nearby buildings to collapse.
提出了液化石油气火灾爆炸事故的预防措施。
The precautionary measures to reduce the explosion and fire of LPG are presented.
从物理性爆炸和化学性爆炸两方面分析了液化石油气罐区发生火灾爆炸的危险，着重就罐区化学性爆炸进行了详细的分析和阐述。
In viewpoint of physical and chemical explosion , fire and explosion hazard was analyzed in LPG tank area. Chemical Explosion was discussed in detail.
从物理性爆炸和化学性爆炸两方面分析了液化石油气罐区发生火灾爆炸的危险，着重就罐区化学性爆炸进行了详细的分析和阐述。
In viewpoint of physical and chemical explosion , fire and explosion hazard was analyzed in LPG tank area. Chemical Explosion was discussed in detail.
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