Fe-MnOx-CeO2/ZrO2低温催化还原NO性能研究

以纳米ZrO2为载体,用浸渍法制备出Fe-MnOx-CeO2/ZrO2催化剂,考察了活性组分配比和助剂负载量对催化剂低温NH3选择性催化还原NO活性的影响,并对催化剂进行了XRD、SEM、EDS和BET表征;探讨了温度、H2O和SO2对Fe-MnOx-CeO2/ZrO2催化剂低温下NH3选择性催化还原NO的影响,结果表明,无SO2和H2O条件下,8%Fe-10%MnOx-CeO2/ZrO2催化剂具有良好的催化活性和稳定性.120℃时,催化剂的脱硝效率为85.23%,当温度升至180℃时,脱硝效率可达到92.0%.SO2和H2O共存条件下,催化剂易失活,采用傅立叶变换红外光谱对各反应阶段的催化剂进行了表征,对其失活机制进行深入研究,结果表明,催化剂失活的主要原因是催化剂表面硫酸铵盐的沉积和催化剂本身活性成分的硫酸盐化.     

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.     

氮氟掺杂二氧化钛(N,F-TiO2)的制备及可见光催化活性的研究

以氨水为氮源,氢氟酸为氟源,采用溶胶-凝胶法制备了氮氟掺杂二氧化钛(N,F-TiO2)光催化剂,并通过X-射线衍射(XRD)和扫描电镜(SEM)技术对其晶型和形态进行表征.最后以酸性红B为模型污染物,探讨了N和F加入量、焙烧温度、焙烧时间、照射时间、催化剂用量、溶液初始浓度和照射功率等因素对N,F-TiO2可见光催化活性的影响.结果表明,制备的N,F-TiO2以锐钛型为主,N和F的掺杂对TiO2的晶相没有明显改变,但可以扩大TiO2的可见光响应范围.当N和F的加入量均为2.0%,且在500℃下焙烧40 min时,得到的N,F-TiO2的可见光催化活性明显高于单N或单F掺杂的TiO2(N-TiO2或F-TiO2).对于50 mL浓度为10.0 mg·L-1的酸性红B溶液,当催化剂加入量为1.5 g·L-1,128W光照3.0 h,溶液pH=5.6时,去除率为85.40%.适当延长光照时间至4.0 h,降解率几乎可达100%.另外,研究还证明了N,F-TiO2催化可见光降解过程中有.OH自由基生成.     

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。     

OMS-2负载Pt催化剂的制备及其催化氧化性能研究

采用前掺杂法、沉积-沉淀法和浸渍法制备了氧化锰八面体分子筛(OMS-2)负载Pt催化剂(Pt/OMS-2),对所制催化剂进行了结构和织构表征。并研究了不同制备方法和沉积-沉淀法中不同制备(Pt负载量和溶液的pH值)对Pt/OMS-2催化氧化CO性能的影响。结果表明,沉积-沉淀法制备的Pt/OMS-2-DP催化剂活性最好(T100=100℃)。这与Pt/OMS-2-DP催化剂中Pt颗粒大小及OMS-2载体与Pt之间存在强相互作用有关。Pt负载量明显影响Pt/OMS-2-DP催化剂的催化活性,3Pt/OMS-2-DP催化剂(Pt=3.0 wt%)催化活性最高,这是由于适当Pt负载量,Pt颗粒较小,并与载体OMS-2的相互作用较强,能较好地活化OMS-2晶格氧。pH值对Pt/OMS-2-DP催化剂催化性能影响较大,这与OMS-2的等电点和Pt在不同溶液中存在不同Pt配位体形式有关。     

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.