CNTs/TiO2/CS光降解苯的动力学

综合光催化氧化苯的动力学过程、光辐射场模型和质量守恒定律,采用平板型反应器建立了碳纳米管/二氧化钛/壳聚糖(CNTs/TiO2/CS)催化薄膜光催化氧化气相苯的数学模型;该模型考虑了光强、相对湿度、初始浓度与气体流速对气相苯光降解的影响。结果表明,建立的数学模型与实验结果吻合较好。     

粗苯污染事故应急处理

针对一次苯泄漏事故的应急处理过程、方法进行论述与总结，并分析了事故现场周围地表、地下水中苯污染浓度的变化情况，提出了该类事故的应急措施，以此作为处理同类事故的参考和依据。     

Seasonal Variation of Toxic Benzene Emissions in Petroleum Refinery

Petroleum refineries are largest chemical industries that are responsible for the emission of several pollutants into the atmosphere. Benzene is among the most important air pollutants that are emitted by petroleum refineries, since they are involved in almost every refinery process. Volatile organic compounds (VOCs) are a major group of air pollutants, which play a critical role in atmospheric chemistry. These contribute to toxic oxidants, which are harmful to ecosystem, human health and atmosphere. The variability of pollutants is an important factor in determining human exposure to these chemicals. The ambient air concentrations of benzene were measured in several sites around the Digboi petroleum refinery, near the city of Gowahati in northeast India, during winter and summer 2004. The seasonal and spatial variations of the ambient air concentrations of this benzene were investigated and analyzed. An estimation of the contribution of the refinery to the measured atmospheric levels of benzene was also performed. The ambient air mixing ratios of benzene in a large area outside the refinery was generally low, in ppbv range, much lower than the ambient air quality standards. This article presents the temporal and spatial variation of air pollution in and around petroleum refinery and showed that no health risk due to benzene is present in the areas adjacent to the refinery.     

胶束形态对十六烷基三甲基溴化铵(CTAB)增溶典型苯系物行为的影响

研究了30℃条件下,浓度为1.2×10-4mol·l-1—2.88×10-2mol·l-1的阳离子表面活性剂十六烷基三甲基溴化铵(CTAB)溶液的吸光度及相应浓度条件时对典型苯系物(苯、甲苯和乙苯)的增溶作用.利用表面活性剂的紫外吸收随浓度变化这一特性,从其不同的拐点处求得CTAB的第一、第二临界胶束浓度分别为7.2×10-4mol·l-1和9.6×10-3mol·l-1.在实验浓度范围内,CTAB溶液对苯、甲苯和乙苯的表观溶解度增溶曲线上同样得到两个拐点,即苯7.2×10-4mol·l-1和9.6×10-3mol·l-1,甲苯7.2×10-4mol·l-1和7.2×10-3mol·l-1以及乙苯7.2×10-4mol·l-1和9.6×10-3mol·l-1,这与第一、第二临界胶束浓度相等或相近.由于溶液中CTAB胶束形态随浓度增加而变化,表明胶束形态对CTAB增溶苯系物的行为有显著影响。     

气相抽提去除红壤中挥发性有机污染物的去污机理探讨

通过探讨土壤气相抽提去除红壤中挥发性有机污染物的去污机理,建立了一维稳态条件下污染物在土壤多孔介质中传质的总微分方程,分别求出了平衡模型和动力学模型的解析解和数值解,并用实验结果对平衡模型和动力学模型进行了模拟和验证.实验结果和模型模拟结果表明理论模型与实验结果吻合良好,平衡模型和动力学模型在描述污染物在土柱通风过程中的传质时,分别适用于不同的阶段.在通风初期平衡模型能够很好地描述实验结果,而随着时间的推移,平衡模型的预测曲线逐渐偏离数据点,到了通风中后期,只有动力学模型才能够较好地描述和预测实验结果.     

电捕法净化焙烧炉沥青烟气

针对炭素焙烧炉烟气特点,采用雾化水预处理和电捕焦油技术,对某炭素厂焙烧炉烟气进行治理,达到既高效净化有害气体,又降低资金投入。处理后的烟气指标为:沥青烟浓度13.8mg/m3,苯并(a)芘浓度0.053×10-3mg/m3,烟尘浓度19.1mg/m3,各项污染物均达标排放。     

Indoor and outdoor BTX levels in Barcelona City metropolitan area and Catalan rural areas

Five aromatic hydrocarbons (benzene, toluene, and three isomeric xylenes) were monitored in indoor and outdoor air of 7 public buildings and 54 private homes, located in Barcelona City metropolitan area and in several rural areas of Catalonia. The sampling was carried out over four periods: spring-summer and winter of 2000, and summer and winter of 2001. Passive ORSA 5 Dra¨ger samplers were used for benzene, toluene, and xylenes (BTX) adsorption. BTX were extracted with carbon disulphide and analysed using ...     

焦化苯初馏份蒸馏釜发生爆炸的原因探讨

通过对某企业的一起典型爆炸事故案例进行分析,找出其产生的原因,提出了预防措施。     

有机化改性海泡石对六六六吸附性能的探讨

分别采用阴阳离子表面活性剂对海泡石进行有机化改性处理,并对改性海泡石进行了吸附六六六实验.结果表明,未经有机化改性的海泡石对六六六各异构体去除能力由小到大依次为:γ-六六六(12.66%)、δ-六六六(12.79%)、α六六六(17.35%)、β-六六六(33.57%).经DOSO3Na有机化改性的海泡石对六六六各异构体的去除能力由小到大依次为:β-六六六、γ δ-六六六、α-六六六.经CTMAB有机化改性的海泡石对六六六各异构体的去除能力由小到大依次为:β-六六六、α-六六六、γ δ-六六六.有机化改性海泡石使体系中β-六六六大幅度增加,可能为有机化海泡石催化α、γ、δ各异构体向β异构体转化.     

生物炭降解苯和甲苯混合废气性能研究

该研究以生物炭为过滤介质 ,探讨过滤塔降解气流中苯、甲苯的生物降解性能 .实验表明 ,在总有机负荷低于 3 5 0 g/ (h·m3)、停留时间 1 5～ 90s的实验条件下 ,滤塔对苯和甲苯混合气体有较好的降解性能 ,苯、甲苯的最大削减能力分别为 1 2 0 g/ (h·m3)和 1 5 0 g/ (h·m3) ,甲苯比苯更易被微生物降解 .滤塔中CO2 生成量随苯、甲苯降解量的增加而增加 ,但实验增长速率小于理论增长速率 .菌落分析表明 ,滤塔中微生物主要有真菌、杆菌、芽孢杆菌 ,其中芽孢杆菌为优势菌种 .根据吸附 生物降解机理 ,建立了VOCs去除模型 ,并予以验证 .