Regeneration of commercial selective catalyst reduction catalysts deactivated by Pb and other inorganic elements

The regeneration of commercial SCR(Selective Catalyst Reduction) catalysts deactivated by Pb and other elements was studied.The deactivated catalyst samples were prepared by chemical impregnation with mixed solution containing K_2SO_4,Na_2SO_4,CaSO_4,Pb(NO_3)_2and NH_4H_2PO_4.A novel method combining Ethylenediaminetetraacetic acid disodium salt(EDTA-2Na) and H_2SO_4solution(viz.catalysts treated by dilute EDTA-2Na and H_2SO_4 solution in sequence) was used to recover the activity of deactivated samples,and the effect was compared with single H_2SO_4,oxalic acid,acetic acid,EDTA or HNO_3 solutions.The surface structure,acidity and reducibility of samples were characterized by N_2adsorption–desorption,inductively coupled plasma optical emission spectrometer(ICP-OES),scanning electron microscopy(SEM),X-ray diffraction(XRD),X-ray fluorescence(XRF),H-2-temperature programmed section(H_2-TPR),NH3-temperature programmed desorption(NH3-TPD) and in situ DRIFTS.Impurities caused a decrease of specific surface area and surface reducibility,as well as Br?nsted acid sites,and therefore led to severe deactivation of the SCR catalyst.The use of an acid solution alone possibly eliminated the impurities on the deactivated catalyst to some extent,and also increased the specific surface area and Br?nsted acid sites and promoted the surface reducibility,thus recovered the activity partially.The combination of EDTA-2Na and H_2SO_4 could remove most of the impurities and improve the activity significantly.The removal of Pb should be an important factor for regeneration.Due to a high removal rate for Pb and other impurities,the combination of EDTA-2Na and H_2SO_4 solutions provided the best efficiency.     

废弃SCR脱硝催化剂无害化处理的研究进展

鉴于废弃SCR脱硝催化剂中含有多种痕量重金属以及可回收利用物质,从处理工艺包括重金属的去除、有价金属的回收等方面综述了废弃SCR脱硝催化剂无害化处理的现状,总结了现阶段的研究重点以及工业化应用的瓶颈。目前主要关注废弃SCR脱硝催化剂中钒、钨、钛的回收工艺,但工业化成本昂贵,难以实现效益均衡化。根据现行废弃SCR脱硝催化剂的处置规范,烟气飞灰中重金属的存在是废催化剂处置工艺复杂化的关键。研究重金属的去除以及有价金属的回收,方能最终实现针对废弃SCR脱硝催化剂无害化处理工艺的综合研发。     

Chemical poison and regeneration of SCR catalysts for NOx removal from stationary sources

Selective catalytic reduction (SCR) of NO_x with NH₃ is an effective technique to remove NO_x from stationary sources, such as coal-fired power plant and industrial boilers. Some of elements in the fly ash deactivate the catalyst due to strong chemisorptions on the active sites. The poisons may act by simply blocking active sites or alter the adsorption behaviors of reactants and products by an electronic interaction. This review is mainly focused on the chemical poisoning on V₂O₅-based catalysts, environmental-benign catalysts and low temperature catalysts. Several common poisons including alkali/alkaline earth metals, SO₂ and heavy metals etc. are referred and their poisoning mechanisms on catalysts are discussed. The regeneration methods of poisoned catalysts and the development of poison-resistance catalysts are also compared and analyzed. Finally, future research directions in developing poisoning resistance catalysts and facile efficient regeneration methods for SCR catalysts are proposed.     

铁基催化剂的微波水热处理对其SCR脱硝性能的影响

利用微波对共沉淀制备的铁铈钛复合氧化物催化剂前驱体进行水热处理,探讨了微波水热处理对铁基催化剂低温SCR脱硝性能的优化;并对微波水热处理条件的影响进行了正交分析.结果表明:对铁基催化剂前驱体进行微波水热处理,可提高其低温SCR脱硝性能,使其脱硝温度窗口向低温偏移;且微波水热处理的低温优化效果与催化剂中Fe/Ti摩尔比密切相关,Fe/Ti摩尔比越小,微波水热处理的低温优化越强;微波加热方式和微波辐射时间会影响微波水热处理对铁基催化剂SCR脱硝性能的低温优化;在相同微波辐射时间条件下,当P30逐渐变为P80,微波水热处理对铁基催化剂低温SCR脱硝的促进作用降低;在P30条件下,微波辐射15min使铁基催化剂具有最佳低温SCR脱硝活性.     

燃煤电站SCR烟气脱硝还原剂尿素热解热源的选择

介绍了燃煤电站SCR尿素热解工艺,结合当前燃料价格,通过工程案例计算,对比了各种尿素热解热源的运行费用。计算结果表明,高温蒸汽加热方案的运行费用最省,但在实际应用中受到相关条件的限制;在一定条件下,燃气加热与电加热方案是工程的优选技术方案。     

The abatement of major pollutants in air and water by environmental catalysis

This review reports the research progress in the abatement of major pollutants in air and water by environmental catalysis. For air pollution control, the selective catalytic reduction of NO _x (SCR) by ammonia and hydrocarbons on metal oxide and zeolite catalysts are reviewed and discussed, as is the removal of Hg from flue gas by catalysis. The oxidation of Volatile organic compounds (VOCs) by photo- and thermal-catalysis for indoor air quality improvement is reviewed. For wastewater treatment, the catalytic elimination of inorganic and organic pollutants in wastewater is presented. In addition, the mechanism for the procedure of abatement of air and water pollutants by catalysis is discussed in this review. Finally, a research orientation on environment catalysis for the treatment of air pollutants and wastewater is proposed.     

玻璃熔窑SCR烟气脱硝设计的影响因素分析

对影响玻璃熔窑SCR烟气脱硝设计的几个主要因素,如烟气条件（烟气量和NOx初始浓度）、还原剂、催化剂、SCR反应器布置方式及催化剂吹灰方式等进行了分析与讨论,指出在对玻璃熔窑进行SCR烟气脱硝设计时应根据燃料情况、烟气条件、生产工艺、环保法规及污染物减排要求等合理进行选择,以确保玻璃熔窑SCR烟气脱硝系统安全运行及工程投资、运行费用的经济合理性。     

江苏省环保资金事前补助金额校正优化研究--以江苏省燃煤发电机组SCR脱硝工程为例

江苏省环保专项资金一般根据专家经验对项目核定后进行事前补助,事后开展针对项目财务支出的合规性评价,但忽视了专家核定补助金额是否合理。根据近3年江苏省燃煤发电机组SCR脱硝工艺典型项目审计报告,分析了项目审计核定支出额与专家核定支出额的规模(100 MW级及以下、300 MW级、600 MW级及以上)差异、区域(苏南、苏中、苏北)差异及其影响因素,发现100 MW级及以下机组环保资金审计核定支出额显著高于专家核定补助额,在剔除100 MW级及以下机组后,苏南地区项目环保资金审计核定支出额显著高于专家核定补助额,基于此提出了项目补助费用校正优化建议,为环保资金科学分配、提高财政资金支出效率提供了理论依据。     

废SCR催化剂中钒和钨的有机酸浸出

在对废SCR催化剂组成进行分析的基础上,采用草酸和酒石酸两种有机酸浸取废SCR催化剂中的V和W。实验结果表明：草酸对V、W的浸出率均大于酒石酸;在草酸浓度为1.00 mol/L、浸取温度为80 ℃、液固比为10 mL/g、浸取时间为180 min时,V和W的浸出率分别为63.50%和13.12%;在酒石酸浓度为0.5 mol/L、浸取温度为100 ℃、液固比为10 mL/g、浸取时间为180 min时,V和W的浸出率分别为44.00%和9.00%。酸性浸出未改变SCR催化剂中TiO₂的晶型,剩余残渣中依然保留着TiO₂骨架,可继续作为催化剂载体使用。     

金属有机骨架材料低温脱硝技术研究进展

金属有机骨架材料（MOFs）因其独特的结构作为催化剂应用于SCR系统表现出较好的低温脱硝效果和较强的抗SO₂、抗H₂O性能。综述了几种较典型的MOFs催化剂及其改性产物的低温催化性能,以及MOFs材料应用于SCR技术的研究进展,指出：对含有两种或两种以上金属的复合MOFs材料的深入研究,是开发稳定性更高、抗SO₂抗H₂O能力更强的MOFs催化剂的重要思路;此外,对有机组成部分进行改性,提高有机配体的热稳定性也是一个重要的研究思路。