磁湖底泥氮释放通量的研究

本研究通过对磁湖底泥氮释放的特性进行实验室静态模拟实验,测定不同温度对磁湖底泥中氮释放量的影响。结果表明,温度升高时,底泥中NH3-N、TN释放通量增大,NO2-N和NO3-N释放通量减小。磁湖底泥的TN释放通量为-120到-25 mg/m3.d,NH3-N、NO2-N和NO3-N和TN释放通量基本呈负释放,说明磁湖大部分氮元素沉积到底泥中。本研究为探讨磁湖水质的改善提供相关的依据,并为以后关于磁湖的治理研究提供一定参考。     

酸化液对厌氧释磷好氧吸磷速率的影响研究

采用序批式试验研究了酸化液对聚磷菌厌氧释磷好氧吸磷速率的影响。同一活性污泥混合液中聚磷菌的释磷潜力相当,混合液中挥发性脂肪酸越多则越有利于激发聚磷菌的释磷潜能。酸化液投加量越大,对应的混合液中聚磷菌的平均释磷速率也越大。当酸化液投加量为30 mg/L(以TOC计)时,聚磷菌的平均释磷速率达0.137 mg/(mg.d),是未投加酸化液工况的3.26倍。聚磷菌厌氧释磷过程中,活性污泥的MLVSS值逐渐增大,而MLSS值却不断减小,这是由聚磷菌释磷反应过程中聚磷颗粒和糖原的消耗,以及PHB的生成而产生的。碳源充足与否,对聚磷菌的平均好氧吸磷速率影响不大,研究各工况中,聚磷菌的平均吸磷速率在0.129~0.160 mg/(mg.d)内。碳源越充足,则聚磷菌在好氧吸磷反应持续的时间越长,因此,具有更强的超量吸磷能力。酸化液投加量为20 mg/L时(以TOC计),聚磷菌在好氧吸磷结束时,出水的SP浓度能减少到0.5 mg/L以下。     

紫色母岩覆盖层控制底泥磷释放的效果及机制

选取重庆地区分布面积较广的3种紫色母岩(飞仙关组、蓬莱镇组和遂宁组),和2种经众多研究证明可有效控制底泥污染物释放的岩石(石灰石和方解石)作为活性覆盖材料,进行底泥覆盖模拟实验,研究紫色母岩覆盖层对底泥磷素释放的控制效果及机制.结果表明,3种紫色母岩覆盖层对底泥总磷向上覆水体释放的抑制作用较强,远好于方解石与石灰石(P0.05).其中,飞仙关组紫色母岩覆盖层对底泥总磷向上覆水体释放的抑制效果最好,抑制率为94.4%.5种覆盖材料均可促进底泥总磷的释放与转化,显著促进底泥OP原位转化为Ca-P,而3种紫色母岩覆盖层更有利于底泥释放出的磷转化为无机磷和有机磷.同时,5种覆盖材料均会改变底泥及上覆水体微生物的群落结构,其中PLFA16:0标记的细菌数量与上覆水体的总磷含量呈显著负相关.     

油品装卸过程静电特性研究

为了研究油品装卸过程中的静电危险性,在两个城市的油库和加油站对油品的装油、卸油过程,以及装油的油罐车从油库向加油站行驶的过程中,油罐车内油品的油面电位进行了静电检测。通过对大量油罐车内油面电位的检测数据分析可以看出,在正常装卸油过程中,油罐车内油品的油面电位远远小于标准所规定安全油面电位,有缩短稳油时间的可能性。     

再悬浮过程中河流底泥PAHs的迁移与释放

利用再悬浮模拟(particle entrainment simulator,PES)装置模拟了河流底泥在受到上层扰动力后的再悬浮过程.结果表明,沉积物性质如粒径组成及PAHs含量对沉积物再悬浮过程中PAHs的释放影响显著.再悬浮过程中上覆水体总悬浮颗粒物(total suspended solids,TSS)含量与颗粒态PAHs之间存在极显著相关关系.切应力对再悬浮过程中PAHs释放的影响体现在两方面.一方面,单位体积的颗粒态PAHs随切应力增大而增大;另一方面,悬浮颗粒上PAHs的富集效应随切应力增大而减弱,是由于切应力强烈导致吸附作用弱的大颗粒进入水体.上覆水体中的PAHs总量在一段时间上升后于120 min或240min趋于稳定,而颗粒态与溶解态之间具有良好响应.高低环PAHs释放行为差异显著,由于中高环PAHs的疏水性,上覆水体中检测到的多为3~4环个体.     

静置/好氧/缺氧序批式反应器（SBR）脱氮除磷效果研究

以静置段代替传统厌氧段,采用后置缺氧方式,考察了静置/好氧/缺氧序批式反应器(SBR)(R1)的生物脱氮除磷(BNR)性能,并与传统厌氧/好氧/缺氧序批式反应器(SBR)(R2)进行对比.两反应器进水乙酸钠、氨氮(NH+4-N)及磷酸盐(PO3-4-P)浓度均分别为350 mg·L-1(以COD计)、40 mg·L-1及12 mg·L-1,水力停留时间(HRT)为12 h.研究结果表明,R1长期运行中磷的去除率与R2相当,分别为92.4%和92.1%,而总氮(TN)去除率则较R2高,分别为83.5%和77.0%.R1静置段省去搅拌但仍能起到厌氧段的作用,为好氧快速摄磷奠定了基础,同时R1缺氧段发生反硝化摄磷,使出水磷降至0.91 mg·L-1.好氧段内R1发生了同步硝化-反硝化(SND),贡献了18.0%的TN去除量,R2也存在SND,但脱氮贡献率较少,仅为9.8%.R1和R2后置缺氧反硝化均以糖原驱动,反硝化速率分别为0.98、0.84 mg·g-1·h-1(以每g VSS产生的N(mg)计),出水TN分别为6.62、9.21 mg·L-1.研究表明,静置段代替传统厌氧段后,可获得更好的脱氮效果,且工艺更为简化.     

南水北调对密云水库水位变幅带土壤磷释放量的影响

南水北调来水引起的水位上涨可能会导致密云水库水位变幅带土壤中磷的释放.过量的磷可能会引起水体富营养,因此,研究水库变幅带磷释放风险对密云水库水质安全保障具有科学指导意义.本研究采用连续浸提法测定密云水库变幅带土壤及沉积物中弱吸附态磷(NH_4ClP)、铁磷(BD-P)、铝磷(NaOH-P)及钙磷(HCl-P)等4种不同形态磷含量,探讨其分布特征;并在室内进行了磷释放模拟实验,估算了南水北调来水引起水库水位上升所致的易释放磷的释放量.结果表明,NH_4Cl-P、BD-P、NaOH-P、HCl-P广泛地分布于密云水库变幅带土壤及沉积物中.在白河、内湖及潮河3个库区,磷形态分布具有一致规律,即HCl-PNaOH-PBD-PNH_4Cl-P.因密云水库变幅带为中国典型的北方碱性土壤,变幅带无机磷主要为钙磷.NH_4Cl-P在3个库区变幅带土壤中含量相差不大,在受水动扰动力影响较小的内湖库区BD-P含量略高于其它2个库区.在3个不同库区中,潜在活性磷NH_4Cl-P和较稳定的NaOH-P在岸上和水陆交界面土壤及水下沉积物中含量相差不大,受氧化还原条件影响较大的BD-P在沉积物中的含量略高于岸上和水陆交界面土壤.磷释放模拟实验及释放量估算结果表明,水库水位上涨3 m的情况下,白河、潮河和内湖库区淹没变幅带土壤分别释放1.02、0.80、0.37 mg·m~(-2)易释放磷.白河和内湖库区变幅带被水淹没土壤中磷释放的风险可能更高,需加强防护.     

底泥中营养物质及其他污染物释放机理综述

水体底泥(沉积物)污染,是世界范围内的一个重要环境问题.其污染物主要通过大气沉降、废水排放、水土流失、雨水淋溶与冲刷进入水体,最后沉积到底泥中并逐渐富集,使底泥受到严重污染.总结了底泥中氨氮、重金属的影响因素及释放机理,也指明了持久性有机污染物释放机理研究不足的现状,提出对其释放机理研究的重要性.     

Morphological characteristics of flashing jet throughout superheated liquid release

Many release problems involve two-phase releases of hazardous materials of superheated liquids with high energy into the atmosphere. Such accidents are accompanied by violent phase transition and form catastrophic flashing jets. In this work, experimental and theoretical analyses were conducted to investigate dynamic characteristics of flashing jet morphology and their dependence on pressure-decay dynamics under different storage pressures, superheats, and nozzle diameters. Flashing jet morphology and angle throughout two-phase releases were captured by a high-speed camera, and the corresponding source pressure in the superheated liquid tank was measured simultaneously. Results show that three typical phases, expansion, stabilization, and decay, are characterized throughout two-phase release based on the evolution of flashing jet morphology. The jet initially expands gradually due to the enhancement of phase transition intensity, and then keeps stable when the intensity reaches its maximum, and terminally decays rapidly due to the depletion of superheated liquid. Phase transition intensity at the nozzle exit is mainly controlled by the pressure-decay dynamics. Bubbles nucleation inception sites gradually move upstream of the nozzle during the pressure decay process increasing the phase transition intensity. The increase of storage pressure, superheat and nozzle diameter promotes the mechanical and thermodynamic effects on the jet breakup. The significant increase of mechanical and thermodynamic effects effectively accelerates droplets evaporation and further affects flashing jet morphology.     

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.