一起钢质无缝气瓶爆炸事故技术分析

文章简要描述了一起消防气体灭火钢质气瓶爆炸事故,对爆炸气瓶进行了断口分析、金相试验和理化试验,并分析了事故的原因,提醒制造厂家规范制造工艺,对预防类似事故的发生具有一定的参考意义。     

污泥负荷对生物处理系统耐药细菌的影响研究

为了研究污水生物处理工艺中抗药性细菌生长和分布特性及污泥负荷的影响,构建了不同处理负荷的活性污泥工艺,并以磺胺嘧啶抗性异养菌为例,阐述了污泥负荷对活性污泥系统中典型抗药细菌的生长及排放特性的影响.结果表明,污泥负荷增大有利于磺胺嘧啶抗性异养菌的生长繁殖,负荷提高后净比生长速率和细菌产量分别由0.32d-1和2.3×106CFU/d提高至0.33d-1和3.1×106CFU/d,活性污泥、出水和剩余污泥中抗药菌的浓度也均显著提高(P < 0.05),但对抗药细菌的相对丰度无显著改变.低污泥负荷下[0.24kg COD/(kg MLSS?d)]抗药细菌主要通过剩余污泥形式排放,排放量比(泥中排放量/水中排放量)为28.4;负荷提高至0.4kg COD/(kg MLSS?d)后,出水抗药细菌排放量显著提高,排放量比为1.1.处理相同水量,高污泥负荷下排放的抗药细菌总量明显降低,提高污泥负荷有利于活性污泥系统抗药性风险的控制.     

Flame-propagation behavior and a dynamic model for the thermal-radiation effects in coal-dust explosions

To reveal the flame-propagation behavior and the thermal-radiation effects during coal-dust explosions, two coal-dust clouds were tested in a semi-enclosed vertical combustion tube. A high-speed video camera and a thermal infrared imaging device were used to record the flame-propagation process and the thermal-radiation effects of the fireball at the combustion-tube outlet. The flame propagated more quickly and with a higher temperature in the more volatile coal-dust cloud. The coal-dust concentration also significantly affected the propagation behavior of the combustion zone. When the coal-dust concentration was increased, the flame-propagation velocity and the fireball temperature increased before decreasing overall. Based on the experimental results, a dynamic model of the thermal radiation was employed to describe the changes in the fireballs quantitatively and to estimate the thermal-radiation effects during coal-dust explosions.     

Duct-venting of dust explosions in a 20 L sphere at elevated static activation overpressures

Ducts are often recommended in the design of dust explosion venting in order to discharge materials to safe locations. However, the maximum reduced overpressure increases in a duct-vented vessel rather than in a simply vented vessel. This needs to be studied further for understanding the duct-venting mechanism. Numerous duct-vented dust explosion experiments were conducted, using a 20 L spherical chamber at elevated static activation overpressures, ranging from 1.8 bar to 6 bar. Duct diameters of 15 mm and 28 mm, and duct lengths of 0 m (simply venting), 1 m and 2 m, were selected. Explosion pressures both in the vessel and in the duct were recorded by pressure sensors, with a frequency of 5 kHz. Flame signals in the duct were also obtained by phototransistors. Results indicate that the secondary explosion occurring in the duct increases the maximum reduced overpressure in the vessel. The secondary explosion is greatly affected by the duct diameter and static activation overpressure, and hence influences the amplification of the maximum reduced overpressure. Larger static activation overpressure decreases the severity of the secondary explosion, and hence decreases the increment in the maximum reduced overpressure. The secondary pressure peak is more obvious as the pressure accumulation is easier in a duct with a smaller diameter. However, the increment of the maximum reduced overpressure is smaller because blockage effect, flame front distortion, and turbulent mixing due to secondary explosion are weaker in a narrow duct. The influence of duct length on the maximum reduced overpressure is small at elevated static activation overpressures, ranging from 1.8 bar to 6 bar at 15 mm and 28 mm duct diameters.     

Limiting explosible concentration of hydrogen–oxygen–helium mixtures related to the practical operational case

This paper presents data on the limiting (minimum) concentrations of hydrogen in oxygen, in the presence of added helium, at elevated temperature and pressure related to the practical operational case. A 5 L explosion vessel, an ignition sub-system and a transient pressure measurement sub-system were used. Through a series of experiments carried out using this system, the limiting concentrations of hydrogen in oxygen and helium at different initial pressures and temperatures for the practical operational case were studied, and the influence of ignition energy and initial temperature on the limiting concentration of hydrogen in oxygen and helium was analyzed and discussed. The variation of ignition energy within the studied range is found to have a significant effect on the limiting concentration of hydrogen in oxygen and helium at lower initial temperature. However, when the ignition energy is higher than 32 mJ, the limiting hydrogen concentration remains almost changeless as the initial temperature increases from 21 °C to 90 °C. The limiting explosible concentration of hydrogen–oxygen–helium mixture decreases as the ignition energy increases when the initial temperature is lower. When the initial temperature is higher, the ignition energy has little effect on the limiting hydrogen concentration of hydrogen–oxygen–helium mixtures. When the initial temperature reaches 90 °C, the limiting hydrogen concentration remains almost changeless with an increase in ignition energy. The limiting explosible concentration of hydrogen in the mixtures, at the initial temperature of 21 °C and the ignition energy of 0.5 mJ, is 8.5% and that of oxygen is 11.25%.     

液氧储罐爆炸事故树分析

采用安全系数工程的方法,对液氧储罐爆炸进行丁事故树分析,通过求事故树最小割集,进行结构重要度分析,从而对液氧储罐爆炸的事故原因进行分析、预测,并提出了相应的预防控制措施。     

环氧乙烷生产系统的安全性评价

用道氏火灾、爆炸危险指数评价方法对抚顺乙烯化工厂环氧乙烷生产系统进行安全性评价.针对环氧乙烷生产系统实际运转情况,对其中的M101混合器单元从一般工艺危险性、特殊工艺危险性和安全补偿措施等方面进行了系统分析,并对该系统的危险性因素进行辨识并提出了相应的整改措施.结果表明,该生产系统中5个评价单元内的实际最大可能财产损失分别是1.407×107元、1.488×107元、0.489×107元、0.804×107元和0.711×107元,均在该评价方法规定的最大可能财产损失范围内,说明现役环氧乙烷生产系统在理论上是可以安全运行的.     

环氧乙烷生产装置的安全分析与评价

综合运用道化学公司火灾、爆炸危险指数评价法,事故树分析以及事件树分析对环氧乙烷生产装置进行安全评价,定量地得出装置的危险程度,定性地分析了各危险因素的大小以及系统中各元件的故障率对事故发生概率的影响程度,并提出了改进措施.结果表明,该装置的危险程度很大,必须加强安全生产管理,采取有效措施控制氧气的浓度,从而降低危险性等级,保证生产安全.     

Continuous biohydrogen production from diluted molasses in an anaerobic contact reactor

An anaerobic contact reactor (ACR) system comprising a continuous flow stirred tank reactor (CSTR) with settler to decouple the hydraulic retention time (HRT) from solids retention time (SRT) was developed for fermentative hydrogen production from diluted molasses by mixed microbial cultures. The ACR was operated at various volumetric loading rates (VLRs) of 20–44 kgCOD·m^-3·d^-1 with constant HRT of 6 h under mesophilic conditions of 35°C. The SRT was maintained at about 46–50 h in the system. At the initial VLR of 20 kgCOD·m^-3·d^-1, the hydrogen production rate dropped from 22.6 to 1.58 L·d^-1 as the hydrogen was consumed by the hydrogentrophic methanogen. After increasing the VLR to 28 kgCOD·m^-3·d^-1 and discharging the sludge for 6 consecutive times, the hydrogentrophic methanogens were eliminated, and the hydrogen content reached 36.4%. As the VLR was increased to 44 kgCOD·m^-3·d^-1, the hydrogen production rate and hydrogen yield increased to 42.1 L·d^-1 and 1.40 mol H₂·molglucose-consumed^-1, respectively. The results showed that a stable ethanol-type fermentation that favored hydrogen production in the reactor was thus established with the sludge loading rate (SLR) of 2.0–2.5 kgCOD·kgMLVSS^-1·d^-1. It was found that the ethanol increased more than other liquid fermentation products, and the ethanol/acetic acid (mol/mol) ratio increased from 1.27 to 2.45 when the VLR increased from 28 to 44 kgCOD·m^-3·d^-1, whereas the hydrogen composition decreased from 40.4% to 36.4%. The results suggested that the anaerobic contact reactor was a promising bioprocess for fermentative hydrogen production.     

我国典型农区耕地承载畜禽容量对比分析

根据农田养分平衡理论,对我国南北两个县级区域山东禹城和湖南桃源的耕地承载畜禽容量和负载指数进行了对比分析。 基于农田N收支情景分析表明:当农田施用粪便N分别占到总投入N的30%、60%和100%时,山东禹城耕地承载畜禽容量分别为4.1、8.3和13.8 LU·hm^-2,相应负载指数分别是2.2、1.1和0.7,湖南桃源耕地承载畜禽容量分别是4.4、8.7和14.6 LU·hm^-2,相应负载指数分别是1.4、0.7和0.4;基于农田N收支的耕地畜禽容量呈现为禹城略低于桃源,负载指数呈现为禹城显著高于桃源。基于农田P收支情景分析表明:当农田施用粪便P₂O₅分别占总施入P₂O₅的30%、60%和100%时,山东禹城耕地承载畜禽容量分别为6.7、13.5和22.5 LU·hm^-2,相应的耕地畜禽承载指数分别是1.3、0.7和0.4,湖南桃源耕地承载畜禽容量分别是2.5、5.1和8.5 LU·hm^-2,相应的负载指数分别是2.4、1.2和0.7,基于农田P收支的耕地畜禽容量呈现为禹城显著高于桃源,负载指数为禹城低于桃源。可见,禹城基于农田N收支的耕地承载畜禽容量显著低于基于农田P收支的耕地承载畜禽容量,桃源正好与禹城相反。因此,今后在制定减少农田环境污染对策时,禹城应首先考虑农田N收支及粪便N的有效管理与利用;桃源则应首先考虑农田P收支及粪便P的有效管理与利用,并且因为区域内乡镇之间存在较大差异,还应在乡镇之间进行协调平衡。