H2S匀圆杂选择性催化氧化工艺及催化剂研究现状

论述了石油流化催化裂化烟气中H2S气体的选择性催化氧化处理工艺和工艺中所使用的各种类型选择性氧化催化剂.目前已发展并投入使用的选择性氧化工艺主要有:Superclaus工艺、Euroclaus工艺、Clinsulf-Do工艺、BSR/Hi-Activity工艺、Selectox工艺和Modop工艺等,各工艺具有不同的特点和应用范围.H2S选择氧化催化剂主要包括以下几种体系:碳体系、SiC载体体系、分子筛体系、氧化物体系和柱撑黏土体系等.其中碳体系和氧化物体系的研究开展的较早较多,关于分子筛体系的研究近期有所减少,SiC是研究人员认为非常有潜力的一个载体体系,其相关体系研究也一直在进行之中,柱撑黏土体系还处于初步研究阶段,离实际应用尚有距离.     

Application of red mud as a basic catalyst for biodiesel production

Red mud was investigated in triglyceride transesterification with a view to determine its viability as a basic catalyst for use in biodiesel synthesis.The effect of calcination temperature on the structure and activity of red mud catalysts was investigated.It was found that highly active catalyst was obtained by simply drying red mud at 200°C.Utilization of red mud as a catalyst for biodiesel production not only provides a cost-effective and environmentally friendly way of recycling this solid red mud waste,significantly reducing its environmental effects,but also reduces the price of biodiesel to make biodiesel competitive with petroleum diesel.     

Formic acid as an alternative reducing agent for the catalytic nitrate reduction in aqueous media

Formic acid was used for the nitrate reduction as a reductant in the presence of Pd:Cu/γ-alumina catalysts. The surface characteristics of the bimetallic catalyst synthesized by wet impregnation were investigated by SEM, TEM-EDS. The metals were not distributed homogeneously on the surface of catalyst, although the total contents of both metals in particles agreed well with the theoretical values. Formic acid decomposition on the catalyst surface, its influence on solution pH and nitrate removal efficacy was investigated. The best removal of nitrate (50 ppm) was obtained under the condition of 0.75 g/L catalyst with Pd:Cu ratio (4:1) and two fold excess of formic acid. Formic acid decay patterns resembled those of nitrate removal, showing a linear relationship between kf (formic acid decay) and k (nitrate removal). Negligible amount of ammonia was detected, and no nitrite was detected, possibly due to buffering effect of bicarbonate that is in situ produced by the decomposition of formic acid, and due to the sustained release of H2 gas.     

半干法烟气脱硫灰改性及应用

文章主要对半干法脱硫灰中亚硫酸钙的氧化转化进行研究。半干法脱硫灰中亚硫酸钙对建材质量具有一定影响,通过筛选合适的催化-氧化剂体系对其进行了氧化改性。试验得到了一种复合催化剂,成功用于半干法脱硫灰改性。结合蒸压砖的生产工艺,使亚硫酸钙在生产过程中实现了部分转化,生产的蒸压砖能达到JC239-2001《粉煤灰砖》MU10强度等级。     

燃煤电厂PM2.5微细颗粒物控制新技术——旋转电极式电除尘性能特点及安装技术

本文介绍了燃煤电厂PM2.5微细颗粒物控制新技术——旋转电极式电除尘器的工作原理、性能特点.同时介绍了某电厂330MW机组旋转电极式电除尘改造工程应用实例.在积累多个旋转电极式电除尘器安装调试经验的基础上,介绍了旋转电极式电除尘器安装工艺流程及安装调试技术.     

Oxidation inhibition of sulfite in dual alkali FGD system

A laboratory-scale well-mixed thermostatic reactor with continuously blasting air was used to investigate the oxidation inhibition of sulfite in dual alkali flue gas desulfurization （FGD） system. The effects of operating parameters such as pH value and catalyst concentration on the oxidation were studied. Sodium thiosulfate was used in the system, and was found that it significantly inhabited the sulfite oxidation. In the absence of catalyst, sodium thiosulfate at 12.67 mmol/L had an inhibition efficiency of approximately 98%. While in the presence of catalyst, sodium thiosulfate at 26.72 mmol/L had an inhibition efficiency less than 85.0%. The oxidation reaction order of sulfite in the sodium thiosulfate was determined to be -1.90 and 4）.55 in the absence and presence of the catalyst, respectively. Apparent activation energy of oxidation inhibition was calculated to be 53.9 kJ/mol. Pilot tests showed that the consumption rate of thiosulfate agreed well with the laboratory-scale experimental results.     

催化剂Ru/ZrO2-CeO2催化湿式氧化苯酚

催化剂Ru/ZrO₂-CeO₂催化湿式氧化苯酚的过程表明,Ru/ZrO₂-CeO₂可以显著提高COD和苯酚去除效果,当反应温度为170℃,压力为3 MPa,反应120 min后,COD和苯酚的去除率分别达到了99％和100％.试验还考察了不同反应条件对苯酚溶液COD去除的影响,并获得了最优的反应条件：温度为170℃,压力为3 MPa,催化剂的投加量为5　g/Ｌ,搅拌速度为500 r/min.通过对中间产物的分析,本研究提出了催化湿式氧化苯酚的简单路径图,认为苯酚首先被氧化成小分子有机酸,接着小分子有机酸被氧化成二氧化碳和水.前一个过程是快速反应,后一个过程中的乙酸氧化是慢速过程,需要在高温下才能完成.乙酸的氧化主要是自由基攻击α碳上的C—H键,先生成甲酸,并最终生成二氧化碳和水.     

Kinetics of selective catalytic reduction of NO by NH3 on Fe-Mo/ZSM-5 catalyst

The catalyst of Fe-Mo/ZSM-5 has been found to be more active than Fe-ZSM-5 and Mo/ZSM-5 separately for selective catalytic reduction (SCR) of nitric oxide (NO) with NH3. The kinetics of the SCR reaction in the presence of O2 was studied in this work. The results show that the observed reaction orders were 0.74-0.99, 0.01-0.13, and 0 for NO, O2 and NH3, respectively, at 350-450℃. And the apparent activation energy of the SCR was 65 kJ/mol on the Fe-Mo/ZSM-5 catalyst. The SCR mechanism was also deduced. Adsorbed NO species can react directly with adsorbed ammonia species on the active sites to form N2 and H2O. Gaseous O2 might serve as a reoxidizing agent for the active sites that have undergone reduction in the SCR process. It is also important to note that a certain amount of NO was decomposed directly over the Fe-Mo/ZSM-5 catalyst in the absence of NH3.     

Pd/C气体扩散电极用于电生成H2O2降解苯酚的研究

采用自制的Pd/C气体扩散阴极和Ti/IrO2/RuO2阳极,在无隔膜电解槽中对苯酚模拟废水降解效果及机制进行了研究,采用电子自旋共振法(ESR)对电解体系中产生的羟自由基(·OH)进行了检测.结果表明,在Pd/C气体扩散体系中掺杂Pd催化剂可以促进H2 O2的生成(H2 O2的稳定浓度是7.5 mg/L),有利于·OH的产生.经电化学氧化处理120 min后,苯酚和COD的去除率分别达到97.2%和50%,表明在电催化氧化过程中苯酚被氧化生成了大量低分子量中间产物.废水的BOD5/COD值达到0.73是处理前的9.1倍,苯酚废水的可生化降解性通过电化学氧化处理后显著提高.在该电化学体系中苯酚的降解是在阳极直接、间接氧化及阴极产生的H2 O2、·OH的氧化共同作用下完成的.通过对紫外扫描光谱图的分析推断出苯酚在电解过程中有醌类物质生成;由GC-MS检测到了邻苯二酚、对苯二酚、苯醌等芳香族化合物和己二酸、顺丁烯二酸、反丁烯二酸、丁二酸、丙二酸、乙二酸等短链羧酸,据此提出了苯酚降解的可能历程.