扰动对悬浮颗粒物粒径及上覆水中磷形态分布的影响

为了探讨底泥扰动下上覆水中悬浮物粒径分布规律及该分布规律对水体中溶解性形态磷的影响,以太湖梅梁湾上覆水和沉积物作为实验对象,开展室内模拟实验.结合乌氏粒级标准分析了扰动下的水体中粒径变化情况以及上覆水中不同磷形态的变化规律.结果表明,扰动后的水体中,悬浮物粒径分布发生明显变化,其中小粒径颗粒(0~10μm)、中粒径颗粒(10~20μm)、大粒径颗粒(≥20μm)的平均占比分别升高、降低、不变.说明中小粒径颗粒物质有向大粒径转化的趋势.另外,在磷形态方面,随着粒径分布的周期性变化,DTP/TP、DIP/TP存在同样的周期性上升规律,数据显示DTP、DIP的变化并不明显,这说明扰动导致悬浮颗粒物对于磷的持留能力提高.另一方面,扰动下DTP/TP和DIP/TP平均值分别为19%和13%,其远低于对照实验(80%和69%),说明扰动引起的小粒径聚集与絮凝成大粒径颗粒的现象有利于上覆水中溶解性形态磷的吸附与沉降,并转化成颗粒态磷,进而延缓水体富营养化的发展进程.     

1997～2004年中国区域经济与火灾态势的关系分析

中国区域经济发展存在较大差异,相应的火灾,隋况也各不相同,本文通过对1997～2004这8年期间的火灾数据的分析,探讨了火灾发展态势在不同地区的特征,并分析了典型地区的火灾和社会经济发展之间的关系。结果表明,当前情况下,随着经济的发展,我国多数地区的火灾发生态势先升高后降低,最后保持平稳;经济较发达的上海地区的火灾发生率已经越过了“最高峰”而趋于平穗好转的时期,此外,同样是经济较发达北京与天津两地的火灾发生率正处于“最高峰”时期,预计在未来几年内其火灾发展将趋于好转。     

太空环境下锂离子电池热失控与火灾的研究展望

综述了锂离子电池的热失控机理,介绍了由于电池内部电解液、电池隔膜和电极材料分解的链式热反应过程而引发的热失控和火灾现象。同时,讨论了锂离子电池在微重力太空环境中可能产生的烟黑浓度倍增,加速火蔓延,火焰喷射等极端火行为。进而探讨了开展锂离子电池的低压、落塔和抛物飞行等地面实验模拟太空微重力燃烧的方法可行性,建立数值模型预测太空微重力环境下锂离子电池热失控临界条件与火灾行为的必要性,以及如何通过基础研究科学地指导空间站电池热管理和消防系统的设计。     

呼吸效应对矿井封闭火区氧浓度的影响分析

为避免因火区封闭导致重大安全事故发生,通过采集某矿井1 d内3个不同监测点的大气压力变化情况,建立大气压力波动模型并分析计算,同时建立火区内外压差100,750 Pa情形下的氧浓度模型进而获得火区内侧氧气浓度因呼吸效应,在不同压差、体积大小火区、风阻、瓦斯涌出量、封闭时刻等多因素耦合影响下随时间的变化规律,以评估火区危险性。研究结果表明:井下大气随地面大气周期波动,封闭火区内、外侧之间的气压差因外界大气波动呈现16 h的余弦波动和8 h的线性波动周期变化;密闭质量好的火区具有更好地抗干扰性,内侧氧浓度的降低主要依靠瓦斯稀释;密闭质量差的火区,内侧氧浓度易受到火区涌出瓦斯、外界涌入大气双重影响;火区氧浓度在2%~12%之间波动,以至火区存在发生瓦斯爆炸的可能性;火区内外压差较大时,氧浓度波动变化幅度更大,危险作用持续时间更长。结合火区氧浓度波动模型,可有效地对矿井火区采取安全的防范措施,避免瓦斯爆炸事故发生。     

Inherent thermal runaway hazard evaluation method of chemical process based on fire and explosion index

Thermal runaway hazard assessment provides the basis for comparing the hazard levels of different chemical processes. To make an overall evaluation, hazard of materials and reactions should be considered. However, most existing methods didn't take the both into account simultaneously, which may lead the assessment to a deviation from the actual hazard. Therefore, an integrated approach called Inherent Thermal-runaway Hazard Index (ITHI) was developed in this paper. Similar to Dow Fire and Explosion Index(F&EI) function, thermal runaway hazard of chemical process in ITHI was the product of material factor (MF) and risk index (RI) of reaction. MF was an indicator of material thermal hazards, which can be determined by initial reaction temperature and maximum power density. RI, which was the product of probability and severity, indicated the risk of thermal runaway during the reaction stage. Time to maximum rate under adiabatic conditions and criticality classes of scenario were used to indicate the runaway probability of the chemical process. Adiabatic temperature rise and heat of the desired reaction and secondary reaction were used to determine the severity of runaway reaction. Finally, predefined hazard classification criteria was used to classify and interpret the results obtained by this method. Moreover, the method was validated by case studies.     

Risk assessment and risk reduction of an acrylonitrile production plant

Reducing accident occurrence in petrochemical plants is crucial, thus appropriately allocating management resources to safety investment is a vital issue for corporate management as international competition intensifies. Understanding the priority of safety investment in a rational way helps achieve this objective.In this study, we targeted an acrylonitrile plant. First, Dow Chemical's Fire and Explosion Index (F&EI) identified the reaction process as having the greatest physical risk. We evaluated the severity of accidents in the reaction process using the Process Safety Metrics advocated by the Center for Chemical Process Safety (CCPS); however, this index does not express damages a company actually experience. To solve this problem, we proposed a new metric that adds indirect cost to CCPS metrics. We adopted fault tree analysis (FTA) as a risk assessment method. In identifying top events and basic events, we attempted to improve the completeness of risk identification by considering accidents from the past, actual plant operation and equipment characteristics, natural disasters, and cyber-attacks and terrorist attacks. Consequently, we identified the top events with high priority in handling because of serious accidents as fire/explosion outside the reactor, fire/explosion inside the reactor, and reactor destruction. The new CCPS evaluation index proposed in this study found that fire and explosion outside the reactor has the highest severity. We considered the creation of the fault tree (FT) diagram of the top event, estimating the occurrence probability, and identifying the risk reduction part and capital investment aimed at risk reduction. As an economically feasible selection method for risk reduction investment, using the difference in loss amounts before and after safety investments indicated investment priority.     

Recent application of Computational Fluid Dynamics (CFD) in process safety and loss prevention: A review

In recent years, significant progress has been made to ensure that process industries are among the safest workplaces in the world. However, with the increasing complexity of existing technologies and new problems brought about by emerging technologies, a strong need still exists to study the fundamentals of process safety and predict possible scenarios. This is attained by conducting the corresponding consequence modeling and risk assessments. As a result of the continuous advancement of Computational Fluid Dynamics (CFD) tools and exponentially increased computation capabilities along with better understandings of the underlying physics, CFD simulations have been applied widely in the areas of process safety and loss prevention to gain new insights, improve existing models, and assess new hazardous scenarios. In this review, 126 papers from 2010 to 2020 have been included in order to systematically categorize and summarize recent applications of CFD for fires, explosions, dispersions of flammable and toxic materials from accidental releases, incident investigations and reconstructions, and other areas of process safety. The advantages of CFD modeling are discussed and the future of CFD applications in this research area is outlined.     

碘量法测定水中溶解氧有关问题的探讨及改进

碘量法测定溶解氧时,采用NH3·H2O—KI代替NaOH(KOH)—KI固定溶解氧,用H2SO4—H3PO(41+1)混合酸代替H2SO4溶解沉淀,使沉淀沉降速度加快,分界线明显,沉淀溶解也更完全。同时做样品空白实验,校正了氧化还原性物质产生的干扰,对废水有明显的抗干扰能力。通过对蒸馏水、自来水、池塘水、废水进行溶解氧测定,结果均非常满意。     

火源位置对L型管廊电缆火灾影响规律的数值模拟研究

选取某城市L型综合管廊电缆舱为研究对象,采用FDS数值模拟软件研究了不同火源位置对L型管廊电缆火灾温度纵向衰减规律、烟气浓度分布规律及烟气危害性的影响。研究结果表明,L型廊道构型影响了不同火源位置的管廊电缆火灾最高温度纵向衰减的连续性,基于热边界层理论提出了适用于L型管廊的二维平面最高温度纵向衰减模型。基于峰宽时间计算了L型管廊火灾的烟气总危害性参数,不同火源位置的烟气危害性总在靠近管廊节点位置处最低。这些结果可对综合管廊的消防设计与火灾防控提供参考。     

风浪扰动对太湖水体重金属形态的影响

对不同风浪条件下水体中的悬浮颗粒物,采用ICP-AES测定其中Co,Cr,Cu,Ni,Pb,Zn,Al,Fe和Mn不同形态的含量.研究表明,水体中Al,Fe,Co,Cr,Pb和Ni可提取态含量随风浪扰动程度的增强其含量均有不同程度的增大. Mn,Zn和Cu在7m·s-1风浪下含量最高,11m·s-1风浪次之,2m·s-1风浪最小.7m·s-1风浪与2m·s-1风浪相比,水体中Mn, Co, Cr, Zn, Cu和Ni的B1, B2, B3态含量增加3-20倍.11m·s-1风浪与7m·s-1风浪相比,Co, Cr和Ni的B1态含量分别增加31.1%-76.8%,Mn, Zn和Cu分别减少22.1%-38.6%; Cr,Zn和Ni的B2态含量增加12.1%-50.2%, Mn减少65.6%, Co和Cu的含量相当; Co和Ni的B3态含量增加15.4%-10.3%,Cr,Mn,Zn和Cu略微减少.水体中的金属主要以Fe-Mn氧化物结合态存在,且金属的三态比例随风浪的变化不明显. Mn的生物有效性最高,Zn,Cu和Ni次之,毒性较大的Pb和Cr的生物有效性较低.Al, Fe和Pb的Fe-Mn氧化物结合态比例非常高,约有74.56%-100%. Co,Cr和Ni的有机结合态比例较高,且Co和 Ni的三态比例比较均一,Cu的B3态较低.