林南仓矿煤低温氧化动力学实验研究

为了研究林南仓矿煤的低温氧化的动力学特性,选取来自不同煤层和采区的3个煤样为实验煤样。通过工业分析和元素分析确定了煤的种类为中高挥发分烟煤,自燃等级为Ⅱ类自燃。分析热重实验结果将低温氧化过程分为失重阶段和增重阶段,确定两阶段为一级化学反应,随着反应深入氧化所需的能量增加。升温氧化实验过程中气体的质量浓度和种类随温度升高而增加,利用电子自旋共振波谱仪研究不同氧化温度下煤中自由基的数量,结果显示自由基浓度出现先减小后增加的趋势。从宏观和微观两个角度提出随着反应程度的加深反应所需能量以及气体产物和自由基数量之间的关系,进一步揭示煤自燃的发展进程。     

二级出水中溶解性有机物亲疏水性对超滤膜污染的影响

利用相对分子质量分布、三维荧光光谱仪及红外光谱仪等方法研究了城市污水二级出水中溶解性有机物亲疏水性对超滤膜污染的影响。结果表明:城市污水二级出水中疏水性酸占42.8%,过渡亲水性酸占19.1%,亲水性有机物占38.1%;水中疏水性酸、过渡亲水性酸和亲水性有机物分别使膜通量减小32.8%、29.9%和18.6%,膜阻力增大106.6%、92.2%和58.6%;过渡亲水性酸为蛋白质类,相对分子质量主要在4000~30000 Da;亲水性有机物为脂肪类,主要集中在6 000 Da以下;疏水性酸物质为腐殖酸类,主要集中在4 000 Da以下,其中疏水性酸物质更容易引起超滤膜污染。     

太湖流域河网4种典型抗生素的时空分布和风险评价

分析了太湖流域人口密度大且养殖业发达的宜溧-洮滆水系水相和沉积相中典型抗生素磺胺甲恶唑(Sulfamethoxazole,SMX)、氧氟沙星(Ofloxacin,OFL)、罗红霉素(Roxithromycin,ROM)和土霉素(Oxytetracycline,OTC)的时空分布特征,并应用商值法进行了健康风险(Health Quotients,HQs)和生态风险(Risk Quotients,RQs)评价.结果表明,宜溧-洮滆水系中OTC、ROM、OFL、SMX在水相的检出率分别为96.5%、57.0%、60.5%和4.5%,沉积相中的检出率分别为96.5%、95.5%、90.0%和44.5%;水相检出浓度最高的抗生素为OTC,最高浓度为17.85 ng·L~(-1);沉积相检出浓度最高的抗生素为SMX,浓度为46.74 ng·g~(-1);相比于其他3种抗生素,流域水相和沉积相中OTC的检出率和检出浓度均较高.宜溧-洮滆水系主要包括南河和长江客水区,丰水期南河水系抗生素的检出水平高于长江客水区.沉积相中抗生素浓度沿水流方向逐渐降低,入湖河口所有点位由于沉积物堆积作用均呈现抗生素富集现象.渔业养殖中抗生素的大量施用是导致该水系抗生素时空分布差异的主要原因.健康风险评价结果表明,4种抗生素均属于可接受风险(HQs0.01).生态风险评价结果表明,4种抗生素均呈现低风险(RQs0.1),其中,生态风险最高的抗生素是OTC,其值为0.086.为有效管控太湖流域抗生素生态风险,应加强对南河水系水产养殖业监管;入湖河口的抗生素富集现象也应引起重视.     

满足国六排放的缸内直喷汽油车污染物排放特性试验研究

以满足国六排放的某缸内直喷轻型汽油车为研究对象,试验研究了该车国六Ⅰ型测试循环(WLTC循环)排放的CO、THC、NOx和固态颗粒数量,以及包含挥发性/半挥发性组分的颗粒物数量和粒径分布特性.结果表明:WLTC循环工况覆盖范围广、车速高、加速度大的特点导致污染物排放增加;车辆冷机起动、暖机过程、瞬态过渡工况和高速大负荷工况对车辆的污染物排放影响较大,研发合理的车辆起动、催化剂起燃和暖机热管理策略、提高发动机瞬态过渡工况响应性是控制排放的重点;包含挥发性/半挥发性组分的颗粒物数量排放呈单峰分布,在15 nm附近达到峰值.     

可靠性评价方法在炼化企业电网中的应用

介绍了国内外电力系统可靠性发展现状,分析了炼化企业生产特点,着重介绍了炼化企业电力系统可靠性评价内容,比较了公用电网与炼化企业的不同性质,说明了二者可靠性评价方法的不同,最后用计算实例说明了可靠性计算方法在炼化企业电力系统中的应用,根据计算结果提出了加强炼化电网可靠性的措施。     

炼化企业被动孤网安稳控制策略关键因素分析

总结了电力行业和炼化企业孤网稳控技术的研究应用现状,分析了炼化企业孤网后的过渡过程,提出了炼化企业孤网稳定控制的关键是频率稳定。根据炼化企业电力系统特点,对影响系统稳定的关键因素,即受控电力负荷和供热机组探讨了建模方法,提出了适用于炼化企业孤网的稳控策略。     

Degradation of sulfonamides and formation of trihalomethanes by chlorination after pre-oxidation with Fe(VI)

Sulfonamides are used in human therapy, animal husbandry and agriculture but are not easily biodegradable, and are often detected in surface water. Sulfamethazine (SMZ) and sulfadiazine (SDZ) are two widely used sulfonamide antibiotics that are used heavily in agriculture. In this study, they were degraded in an aqueous system by chlorination after pre-oxidation with ferrate(VI) (Fe^VIO₄^2 ?, Fe(VI)), an environmentally friendly oxidation technique that has been shown to be effective in degrading various organics. The kinetics of the degradation were determined as a function of Fe(VI) (0–1.5 mg/L), free chlorine (0–1.8 mg/L) and temperature (15–35°C). According to the experimental results, SMZ chlorination followed second-order kinetics with increasing Fe(VI) dosage, and the effect of the initial free chlorine concentration on the reaction kinetics with pre-oxidation by Fe(VI) fitted a pseudo-first order model. The rate constants of SDZ and SMZ chlorination at different temperatures were related to the Arrhenius equation. Fe(VI) could reduce the levels of THMs formed and the toxicity of the sulfonamide degradation systems with Fe(VI) doses of 0.5–1.5 mg/L, which provides a reference for ensuring water quality in drinking water systems.     

Degradation of sulfonamides and formation of trihalomethanes by chlorination after pre-oxidation with Fe(Ⅵ)

Sulfonamides are used in human therapy,animal husbandry and agriculture but are not easily biodegradable,and are often detected in surface water.Sulfamethazine(SMZ) and sulfadiazine(SDZ) are two widely used sulfonamide antibiotics that are used heavily in agriculture.In this study,they were degraded in an aqueous system by chlorination after pre-oxidation with ferrate(VI)(FeVIO42-,Fe(VI)),an environmentally friendly oxidation technique that has been shown to be effective in degrading various organics.The kinetics of the degradation were determined as a function of Fe(VI)(0–1.5 mg/L),free chlorine(0–1.8 mg/L) and temperature(15–35°C).According to the experimental results,SMZ chlorination followed second-order kinetics with increasing Fe(VI) dosage,and the effect of the initial free chlorine concentration on the reaction kinetics with pre-oxidation by Fe(VI) fitted a pseudo-first order model.The rate constants of SDZ and SMZ chlorination at different temperatures were related to the Arrhenius equation.Fe(VI) could reduce the levels of THMs formed and the toxicity of the sulfonamide degradation systems with Fe(VI) doses of 0.5–1.5 mg/L,which provides a reference for ensuring water quality in drinking water systems.     

Nitrous oxide generation in denitrifying phosphorus removal process: main causes and control measures

Despite the many benefits of denitrifying phosphorus removal process, the significant generation of nitrous oxide (N₂O), a potent greenhouse gas, remains a problem for this innovative and promising process. To better understand and more effectively control N₂O generation in denitrifying phosphorus removal process, batch experiments were carried out to investigate the main causes of N₂O generation, based on which the control measures were subsequently proposed. The results showed that N₂O generation accounted for 0.41 % of the total nitrogen removal in denitrifying phosphorus removal process, whereas, in contrast, almost no N₂O was generated in conventional denitrification process. It was further demonstrated that the weak competition of N₂O reductase for electrons and the high nitrite accumulation were the two main causes for N₂O generation, evidenced by N₂O production and reduction rates under different conditions. Accordingly, the reduction of N₂O generation was successfully achieved via two control measures: (1) the use of continuous nitrate addition reducing N₂O generation by around 91.4 % and (2) the use of propionate as the carbon source reducing N₂O generation by around 69.8 %.