两级完全混合发酵工艺开发碳源试验研究

采用两级完全混合发酵工艺进行碳源开发试验,研究了水力停留时间(HRT)和污泥停留时间(SRT)对工艺开发碳源效果的影响.研究表明,固定SRT为4d,污泥回流比为1,HRT在32~36h,系统出水的溶解性COD(SCOD)可维持在1090~1180mg/L,且浓缩池泥水分离效果较好,出水的SS保持在50~80mg/L.保持系统的HRT为32h,污泥回流比为1,SRT在4~7d时,可实现厌氧系统中产酸菌与产甲烷菌的分离,系统能够保持良好的产酸效果,此时系统出水的SCOD值基本稳定于980~1179mg/L.碱度可以作为衡量水解酸化系统是否有效运行的重要参数.HRT为32h,SRT为4d的工况下,初沉污泥酸化发酵系统对氨氮和磷的释放率分别为3.88 mgN/gVSS和0.27mgP/gVSS.     

厌氧、缺氧、好氧环境下富磷剩余污泥的释磷机制

以采用A/O生物强化除磷工艺水质净化厂排出的富磷剩余污泥为研究对象,利用棕色消化瓶设计3组释磷试验,讨论厌氧、缺氧、好氧环境下富磷剩余污泥消化释磷的机制. 结果表明:富磷剩余污泥在厌氧和缺氧环境下均有明显的释磷现象,平均释磷速率分别为1.614和0.998 mg/(L·d);厌氧和缺氧环境下释磷量与聚β-羟基丁酸(PHB)之间的计量关系比较表明,释磷过程中包含有明显的微生物释磷机制,同时还存在着物理化学方面引起的释磷机制,硝酸盐抑制剩余污泥中磷的释放主要是通过影响其微生物学机制完成的.      

沉水植物衰亡过程中营养盐的释放过程及规律

在实验室模拟条件下研究了常见沉水植物苦草、金鱼藻在自然衰亡过程中主要营养盐氮、磷的释放过程,探索沉水植物衰亡过程中营养盐的释放规律. 结果表明:秋、冬季低温条件下,苦草、金鱼藻逐渐衰亡腐败,该过程向水体中释放的氮、磷很少,大部分氮、磷保留在植物残体中. 至次年天气回暖后,植物体的腐败分解有所加快,向水体释放氮、磷并有部分氮、磷沉积进入底泥. 苦草、金鱼藻具有较低的分解速度,有利于降低系统中氮、磷的循环速度. 残留植物体的生物量可影响植物体的分解速度和程度,较大的生物残留量会引起水体缺氧,植物残体分解加剧,导致水质严重恶化.      

模拟酸雨下H+-Ca2+在红壤表面的动力学特征

研究模拟酸雨下H Ca2 在红壤表面的反应动力学吸附特征 ,结果表明 :Ca2 的吸附动力学能很好地用一级动力学方程、抛物线扩散方程和Elovich方程 (R2 >0 97)拟合 .随溶液酸度的增加 ,Ca2 的最大吸附量显著降低 ,Ca2 吸附反应速率控制步骤是离子在颗粒内的扩散 ,扩散速率常数随酸度的增加而下降 .酸溶液pH值为 4 5和 5 6时 ,有H 的释放 ,H 的表观释放量能用一级动力学方程和扩散方程拟合 ,Elovich方程不宜拟合pH 5 6酸处理的动力学数据 ;酸溶液pH值为 3 5和 2 5时 ,有H 的消耗 ,H 消耗总量看作表观消耗量 ,用一级动力学方程、Elovich方程和扩散方程进行拟合 .比较相关系数和标准误差的大小 ,除pH值为 2 5的酸处理用扩散方程拟合结果较差外 ,这 3种动力学模型进行拟合均得到较满意的结果     

燃煤氟中毒地区民用高氟煤的氟释放规律

实验室模拟实验和农户家中的现场测定表明,室内空气氟含量与民用煤的氟含量呈正相关趋势(R=0.612, p<0.01);但在民用炉燃烧温度条件下的煤氟释放率却与煤氟含量无关.在200～1200℃范围内,煤氟释放率随温度的变化曲线呈"S"型,即300℃时开始逐渐上升,700℃前较低,最高不超过31%,700℃至1000℃之间,则释放率迅速上升,随后较为缓慢,到1100℃至1200℃时,释放率接近100%,其整个释放曲线可用Logistic方程来拟合.总体上,煤氟释放与煤氟的存在状态和煤中的矿物及化学组成有关,贵州烟煤、无烟煤氟的燃烧释放要比陕南石煤更快,前者的释放率在1100℃时就接近100%,而后者则到1200℃时才释放完全.民用炉的燃烧温度最高为1000℃左右,这时贵州烟煤、无烟煤样品的平均氟释放率为86.9%,而陕南石煤样品的平均氟释放率为80.6%.     

Risk analysis of a cross-regional toxic chemical disaster by using the integrated mesoscale and microscale consequence analysis model

The rapidly growing capacity and scale of the world's petrochemical industries have forced many plants to have an even larger amount of hazardous substances. Once a serious leak occurs, the outcome of the effect zone could be very large or even uncontrollable just like the Bhopal disaster. In order to assess the risk of a cross-regional damage, this study aims to develop a model that can combine the benefits of both CFD model of the microscale simulation and the Gaussian dispersion model of the mesoscale simulation.The developed integrated model is employed on a toxic chemical tank leak accident of a process plant within an industrial park in order to explore the consequences and the risk of the toxic gas dispersion on three different scopes; one is the accident site, the second is the long-distance transmission route of the mesoscale area and the third is a target city. According to the simulation's results, it is obvious that the complexity of the structure surrounding the leaking tank will eventually affect the maximum ground concentration, the cloud shapes and cloud dilution rate, while the released gas is under dispersion. On the other hand, since the simple Gaussian dispersion model doesn't consider the above impacts, its calculation results will have many differences as compared to the realistic situation. This integrated model can be used as a tool for estimating the risk on a microscale or mesoscale areas and it can produce better results when an environmental impact analysis is required for a larger hazardous chemical process.     

居室装修后空气中甲醛、三苯释放规律及防治对策

对装修后居室中的甲醛、三苯释放浓度进行了监测分析,找出了甲醛、三苯的释放规律,提出装修后的居室应注意通风,保持空气流畅,停留一段时间再入住等对策,以避免室内甲醛、三苯释放,危害人体健康。     

An innovative and comprehensive approach for the consequence analysis of liquid hydrogen vessel explosions

Hydrogen is one of the most suitable solutions to replace hydrocarbons in the future. Hydrogen consumption is expected to grow in the next years. Hydrogen liquefaction is one of the processes that allows for increase of hydrogen density and it is suggested when a large amount of substance must be stored or transported. Despite being a clean fuel, its chemical and physical properties often arise concerns about the safety of the hydrogen technologies. A potentially critical scenario for the liquid hydrogen (LH₂) tanks is the catastrophic rupture causing a consequent boiling liquid expanding vapour explosion (BLEVE), with consequent overpressure, fragments projection and eventually a fireball. In this work, all the BLEVE consequence typologies are evaluated through theoretical and analytical models. These models are validated with the experimental results provided by the BMW care manufacturer safety tests conducted during the 1990's. After the validation, the most suitable methods are selected to perform a blind prediction study of the forthcoming LH₂ BLEVE experiments of the Safe Hydrogen fuel handling and Use for Efficient Implementation (SH₂IFT) project. The models drawbacks together with the uncertainties and the knowledge gap in LH₂ physical explosions are highlighted. Finally, future works on the modelling activity of the LH₂ BLEVE are suggested.     

霉变对储存水稻燃烧行为影响的研究

储存水稻火灾危险性研究具有重要意义。通过研究霉变对储存水稻燃烧行为的影响,确定其火灾危险性。锥形量热燃烧实验(Cone Test)结果显示,霉变样品可以在更小的外加辐射下被点燃;在四种热辐射(25 kW/m2,35 kW/m2,45 kW/m2,55 kW/m2)下,霉变样品的着火时间(TTI)与火灾性能指数(FPI)均小于未霉变样品;而火灾蔓延指数(FGI)高于未霉变样品。Cone Test结果表明霉变显著提高了储存水稻的火灾危险性。差示扫描量热仪(DSC)测试发现在低温时霉变样品比未霉变时吸热焓值提高了3.6倍,表明其析出了更多的小分子挥发物。结合气相质谱联用(GC-MS)测试确定了霉变样品析出的挥发物中含有醇类, 酯类和醛类等易燃物。采用稳态管式炉(SSTF)进一步研究储存水稻的充分燃烧行为,结果显示热释放量及烟气毒性与样品质量(20 g,40 g)以及一次进气量(10 L/min,20 L/min,30 L/min)有关,霉变对于两者的影响较小。     

液化石油气站装卸连接装置改造的安全隐患分析

针对目前液化石油气站内装卸软管已强制要求改装为液体装卸臂的现状,本文梳理了原质监部门和安监部门对液化石油气站内装卸连接装置的不同要求,对在用液体装卸臂改造存在的安全隐患和后续的监管问题进行了分析,并对液体装卸臂的改造和监管提出了几点建议.