光催化氧化法处理染料中间体H酸水溶液

为了去除水中难氧化的有害染料中间体Ｈ酸,研究以ＴＩＯ２、ＺｎＯ、ＣｄＳ和Ｆｅ２Ｏ３为催化剂,采用低压汞灯为光源,对Ｈ酸水溶液进行光催化氧化实验．结果表明：ＴｉＯ２和ＣｄＳ的催化效果最好．采用ＴｉＯ２作催化剂,光催化氧化５ｈ后,Ｈ酸分解率可达９０％,反应速率遵从Ｌａｎｇｍｕｉｒ－Ｈｉｎｓｈｅｌｗｏｏｄ方程,Ｋ＝１２．３Ｌ／ｍｍｏｌ,ｋ＝２５．２×１０－６ｍｏｌ／ｈ．溶液中投加１０ｍｇ／Ｌ的Ｆｅ３＋或Ａｇ＋,可使反应时间缩短２—３ｈ．研究探讨了ｐＨ、ＴｉＯ２投加量和Ｈ酸浓度对催化氧化过程的影响．     

我国氮氧化物排放因子的修正和排放量计算:2000年

根据我国城市的发展状况 ,采用城市分类的方法 ,将我国 2 6 1个地级市按照人口数量分为 5个类别。每类城市选取一个典型城市进行实地调查 ,对我国燃烧锅炉和机动车的NOx 的排放因子进行了修正 ,提出了适合我国目前排放水平的各类城市的固定源和移动源的排放因子。并依据 2 0 0 0年中国大陆地区的电站锅炉、工业锅炉和民用炉具的燃料消耗量和机动车保有量 ,以地级市为基本单位 ,估算了 2 0 0 0年我国各地区的NOx 排放量 ,分析了分地区、分行业、分燃料类型的NOx 排放特征。 2 0 0 0年我国NOx 排放总量为 11.12Mt,其中固定源占 6 0 .8% ;移动源占 39.2 %。NOx 排放在地域、行业和燃料类型上分布均不平衡。NOx 的排放主要集中在华东和华北地区 ,其排放量占全国排放量的一半以上。燃煤为最重要的NOx 排放源 ,其排放量占燃料型NOx 排放量的 72 .3%左右。     

Ag-Al2O3催化剂选择性催化还原稀薄燃烧NOx的研究

本研究主要考察了丙烯为还原剂 ,溶胶 凝胶和共沉淀两种方法制备的Ag Al2 O3催化剂的活性 ,实验结果表明Ag(5 ) Al2 O3(SG)催化剂具有最高的活性。同时详细考察了C3H6 浓度、NO浓度和空速等因素对Ag(5 ) Al2 O3(SG)催化剂活性的影响 ,实验结果表明该催化剂在高空速条件下仍然具有良好的性能。此外 ,还考察了乙烯、丙烷和辛烷为还原剂 ,Ag(5 ) Al2 O3(SG)催化剂的活性 ,实验结果表明以辛烷为还原剂 ,该催化剂还原NOx 的活性 ,特别是低温活性明显提高     

二氧化钛的改性及其对降解水中有机污染物的促进作用

综述了TiO2光催化剂的改性方法及其对光催化降解水中有机污染物的促进作用,介绍了复合物、煅烧温度、掺杂量、掺杂金属离子的种类和浓度对TiO2光催化性能的影响。     

Precise regulation of acid pretreatment for red mud SCR catalyst: Targeting on optimizing the acidity and reducibility

• The optimum SCR activity was realized by tuning the acid pretreatment. • Optimized catalysts showed NO_x conversion above 90%. • The NH₃ and NO adsorption capacity of Al-O₃-Fe is stronger than Fe-O₃-Fe. • The formation of almandine consumes Fe³⁺ and Al³⁺ and weakens their interaction. Red mud (RM), as an alkaline waste, was recently proved to be a promising substitute for the SCR catalyst. Dealkalization could improve the acidity and reducibility of red mud, which were critical for SCR reaction. However, the dealkalization effect depended on the reaction between acid solution and red mud. In this study, we realized the directional control of the chemical state of active sites through tuning the acid pretreatment (dealkalization) process. The pretreatment endpoint was controlled at pH values of 3–5 with diluted nitric acid. When the pH values of red mud were 3 and 5 (CRM-3 and CRM-5), activated catalysts showed NO_x conversion above 90% at 275°C–475°C. The high initial reaction rate, Ce³⁺/(Ce³⁺ + Ce⁴⁺) ratio, and surface acidity accounted for the excellent SCR performance of CRM-5 catalyst. Meanwhile, more Fe³⁺ on the CRM-3 surface improved the NH₃ adsorption. There was a strong interaction between Al and Fe in both CRM-5 and CRM-3 catalysts. DFT results showed that the adsorption capacity of the Al-O₃-Fe for NH₃ and NO is stronger than that of Fe-O₃-Fe, which enhanced the NO_x conversion of the catalyst. However, the almandine was formed in CRM-4, consumed part of Fe³⁺ and Al³⁺, and the interaction between Al and Fe was weakened. Also, deposited almandine on the catalyst surface covered the active sites, thus leading to lower NH₃-SCR activity.