焊接工艺多源散发的高温颗粒污染物扩散特性数值模拟

为探究热工艺过程产生的热气流作用下颗粒的迁移规律,基于气固两相离散粒子模型(DPM)对多源浮射流伴生的高温颗粒的扩散特性进行了数值研究,讨论了两相流运动过程中热气流与颗粒群的温度和速度的瞬时变化情况.结果表明,对于473K£T₀£673K的高温颗粒群,温度衰减趋势类似,颗粒群温度分布呈中心对称;当5μm£d_p£20μm时,颗粒与气流之间的跟随性随着粒径的增大而降低;热羽流随时间经历了独立发展和相互合并的过程,羽流之间涡旋结构的消失导致中心位污染源散发的d_p=10μm的颗粒更容易发生沉降.     

碳中和趋势下数学模拟在污水处理系统中的发展与综合应用

数学模拟技术在污水处理方面被广泛应用,为了系统总结相关技术,本文回顾了污水处理系统中数学模拟技术的发展历程;综述了活性污泥模型(ASM)与机器学习(ML)在水质预测及参数工况优化领域中的应用;重点探究了污水处理系统中温室气体排放模型,以及多目标优化模型在污水处理系统中温室气体排放(GHG)、出水质量(EQI)和运行成本(OCI)的权衡问题;归纳了数学模拟技术在实现污水厂能量自给与资源回收的应用发展.研究结果表明数学模拟技术能准确预测出水水质、快速优化工艺参数、权衡温室气体排放、出水水质与运行成本之间的关系、以及提高资源回收效率等.因此,数值模拟技术可有效指导污水处理工艺的运行优化以及管理,为污水处理行业减污降碳协同增效提供技术支撑.     

生物酶对初沉污泥厌氧发酵产短链脂肪酸的调控研究

旨在通过生物酶调节(碱性蛋白酶、中性蛋白酶和α-淀粉酶)提高初沉污泥的厌氧发酵效率,并通过微生物群落结构解析,SCFAs (short-chain fatty acids,SCFAs)组分分析等揭示其调控机理.结果表明,3种生物酶均可增强初沉污泥水解和产酸作用,碱性蛋白酶调控系统对初沉污泥厌氧发酵的促进效果最为明显,发酵第4d SCFAs的产量和产率分别达到1508mg COD/L和0.174g COD/g VSS.对比控制组,SCFAs的产量和产率分别增加了1129mg COD/L和0.13g COD/g VSS.微生物群落结构分析表明,在碱性蛋白酶调控发酵系统中,Lentimicrobium、Proteiniphilum和Bacteroides等发酵相关菌群的相对丰度得到了改善,Methanosaeta、Methanospirillum等产甲烷古菌的活性受到了抑制.同时,生物酶调控对促进发酵过程乙酸占比也有促进作用.     

FeS对CW-MFC系统降解活性艳红X-3B效果及过程的影响

在自行构建的人工湿地-微生物燃料电池(CW-MFC)系统中,以砾石填料为对照,研究了FeS对活性艳红X-3B脱色效果及降解过程的影响.结果表明,加在底层区域的FeS能够显著提高CW-MFC对活性艳红X-3B的脱色效果和系统产电性能.FeS的投加使得系统脱色率在进水活性艳红X-3B浓度200mg/L、葡萄糖浓度100mg/L条件下达到99.83%.在进水活性艳红X-3B浓度100mg/L、葡萄糖浓度200mg/L条件下,FeS组最大功率密度达到0.849W/m³.活性艳红X-3B在系统中的脱色主要发生在底层和阳极区域,由紫外-可见全波长扫描图谱和GC-MS扫描图谱可知FeS在该区域促进了偶氮双键的断裂,并有利于脱色产物苯胺、三嗪结构、萘环结构的进一步降解.     

低NOx环境异戊二烯促进甲苯生成甲基丁烯二醛的模拟实验

在低NO_x浓度条件下开展甲苯和异戊二烯复合体系的烟雾箱模拟实验,使用高时间分辨率的在线质子转移反应飞行时间质谱(PTR-TOF-MS)实时监测混合体系中反应物与产物的浓度变化情况,探究人为源与天然源交汇过程中, 自然源挥发性有机物 (BVOCs)对人为挥发性有机物(AVOCs)化学降解的影响.结果表明,异戊二烯与甲苯竞争OH自由基,从而抑制了甲苯的化学降解,该竞争反应开始得越早,抑制效果越显著.研究还发现异戊二烯会增强甲苯RO₂降解途径产物的产量,生成更多1,4不饱和-二羰基化合物(如丁烯二醛和甲基丁烯二醛)与二羰基化合物(如乙二醛和甲基乙二醛),其中甲基丁烯二醛增量最高可达38.6%.此外,异戊二烯快速氧化生成的RO₂自由基碳数更少,可能与甲苯氧化生成的RO₂自由基发生了快速的交叉反应,有利于甲苯RO自由基的生成及裂解,最终导致甲苯RO₂途径裂解产物的增加.     

铁盐浸渍强化污泥活性炭-甲醇热质传递特性

针对以市政污泥为核心的炭素前驱体开展原位铁盐浸渍磁修饰,通过响应曲面试验设计优化并制备了新型原位浸渍炭IM-WNC;以成品炭的后浸渍磁修饰炭PM-WNC为参比,考察了原位浸渍与后浸渍磁修饰过程对污泥活性炭-甲醇工质对的吸附/解吸速率、吸附等温线、吸附床传热性能、制冷量及制冷功率等方面的影响。结果表明:与后浸渍过程相比,原位铁盐浸渍有利于保持污泥炭总孔容积(0.6608cm³/g)及比表面积(1122m²/g)水平,能显著提升致密化污泥炭IM-WNC的导热系数(600kg/m³,4.586W/(m·K))、甲醇Sokoda&Suzuki平衡吸附量((528.74±15.86)mg/g)和Langmuir最大吸附量((673.99±13.52)mg/g)。升温脱附与冷却吸附循环体系内,IM-WNC致密化吸附床中心温度峰谷差值可达到69.07℃。当循环时间为76min,解吸温度为100℃时,IM-WNC吸附制冷床的制冷量和制冷功率分别达到501.43kJ/kg和799.06kJ/(kg·h),较PM-WNC分别提升了15.61%和18.69%。     

A novel approach to estimate and control denitrification performance in activated sludge systems with respirogram technology

Respirogram technology has been widely applied for aerobic process, however, the response of respirogram to anoxic denitrification is still unclear. To reveal such response may help to design a new method for the evaluation of the performance of denitrification. The size distribution of flocs measured at different denitrification moments demonstrated a clear expansion of flocs triggered by denitrification, during which higher specific endogenous and quasi-endogenous respiration rates (SOUR_e and SOUR_q) were also observed. Furthermore, SOUR_q increases exponentially with the specific denitrification rate (SDNR), suggesting that there should be a maximum SDNR in conventional activated sludge systems. Based on these findings, an index R_q/t, defined as the ratio of quasi-endogenous (OUR_q) to maximum respiration rate (OUR_t), is proposed to estimate the denitrification capacity that higher R_q/t indicates higher denitrification potential, which can be readily obtained without complex measurement or analysis, and it offers a novel and promising respirogram-based approach for denitrification estimation and control by taking measures to extend anoxic time to maintain its value at a high level within a certain range.     

Dosing low-level ferrous iron in coagulation enhances the removal of micropollutants, chlorite and chlorate during advanced water treatment

Drinking water utilities are interested in upgrading their treatment facilities to enhance micropollutant removal and byproduct control. Pre-oxidation by chlorine dioxide (ClO₂) followed by coagulation-flocculation-sedimentation and advanced oxidation processes (AOPs) is one of the promising solutions. However, the chlorite (ClO₂^–) formed from the ClO₂ pre-oxidation stage cannot be removed by the conventional coagulation process using aluminum sulfate. ClO₂^– negatively affects the post-UV/chlorine process due to its strong radical scavenging effect, and it also enhances the formation of chlorate (ClO₃^–). In this study, dosing micromolar-level ferrous iron (Fe(II)) into aluminum-based coagulants was proposed to eliminate the ClO₂^– generated from ClO₂ pre-oxidation and benefit the post-UV/chlorine process in radical production and ClO₃^– reduction. Results showed that the addition of 52.1-µmol/L FeSO₄ effectively eliminated the ClO₂^– generated from the pre-oxidation using 1.0 mg/L (14.8 µmol/L) of ClO₂. Reduction of ClO₂^– increased the degradation rate constant of a model micropollutant (carbamazepine) by 55.0% in the post-UV/chlorine process. The enhanced degradation was verified to be attributed to the increased steady-state concentrations of HO^· and ClO^· by Fe(II) addition. Moreover, Fe(II) addition also decreased the ClO₃^– formation by 53.8% in the UV/chlorine process and its impact on the formation of chloro-organic byproducts was rather minor. The findings demonstrated a promising strategy to improve the drinking water quality and safety by adding low-level Fe(II) in coagulation in an advanced drinking water treatment train.     

Potassium ferrate pretreatment promotes short chain fatty acids yield and antibiotics reduction in acidogenic fermentation of sewage sludge

During the acidogenic fermentation converting waste activated sludge (WAS) into short-chain fatty acids (SCFA), hydrolysis of complex organic polymers is a limiting step and the transformation of harmful substances (such as antibiotics) during acidogenic fermentation is unknown. In this study, potassium ferrate (K₂FeO₄) oxidation was used as a pretreatment strategy for WAS acidogenic fermentation to increase the hydrolysis of sludge and destruct the harmful antibiotics. Pretreatment with K₂FeO₄ can effectively increase the SCFA production during acidogenic fermentation and change the distribution of SCFA components. With the dosage of 0.2 g/g TS, the maximum SCFA yield was 4823 mg COD/L, which is 28.3 times that of the control group; acetic acid accounts for more than 90% of the total SCFA. The higher dosage (0.5 g/g TS) can further increase the proportion of acetic acid, but inhibit the overall performance of SCFA production. Apart from the promotion of hydrolysis and acidogenesis, K₂FeO₄ pretreatment can also simultaneously oxidizes and degrades part of the antibiotics in the sludge. When the dosage is 0.5 g/g TS, the degradation efficacy of antibiotics is the most significant, and the contents of ofloxacin, azithromycin, and tetracycline in the sludge are reduced by 69%, 42%, and 50%, respectively. In addition, K₂FeO₄ pretreatment can also promote the release of antibiotics from sludge flocs, which is conducive to the simultaneous degradation of antibiotics in the subsequent biological treatment process.     

Enhancing anoxic denitrification of low C/N ratio wastewater with novel ZVI composite carriers

External organic carbon sources are needed to provide electron donors for the denitrification of wastewater with a low COD/NO₃^--N（C/N） ratio, increasing the treatment cost. The economic strategy is to enhance the bioactivity and/or biodiversity of denitrifiers to efficiently utilize organic substances in wastewater. In this study, novel zero-valent iron（ZVI） composite carriers were prepared and implemented in a suspended carrier biofilm reactor to enhance the bioactivity an...