Font Size: a A A

Study On MnCeTiOx Catalyst For Hg0 Catalytic Oxidation And NH3 Selective Catalytic Reduction Of NO In Flue Gas

Posted on:2023-01-26Degree:MasterType:Thesis
Country:ChinaCandidate:H LiuFull Text:PDF
GTID:2531306821995139Subject:Chemical Engineering and Technology
Abstract/Summary:PDF Full Text Request
Currently,coal is still the most consumed energy source in our country,and its combustion produces nitrogen oxides(NOx),sulfur dioxide(SO2),dust,and heavy metals such as mercury,which cause serious air pollution problems.NOx initiates many climate hazards such as acid rain,photochemical smog,and ozone layer damage.Mercury has highly toxic,migratory,and bioaccumulative,making it one of the major air pollutants of concern.The efficient removal of NOx and Hg0 is one of the focused topics in the current environmental field.At present,the most practical and efficient NOx removal technology is ammonia selective catalytic reduction(NH3-SCR)technology,and the core of this technology is the SCR catalyst.Numerous studies presented that SCR catalysts also have the effect of catalytic oxidation of Hg0.The SCR catalysts can oxidize Hg0 to Hg2+.The subsequent pollutant treatment devices can remove Hg2+eastos to achieve the removal of Hg0.Therefore,it is an efficient and economical method to realize the simultaneous removal of NOx and Hg0 by using the SCR denitration device.However,the existing commercial SCR catalyst has a high thigh-temperaturew.The denitration device is arranged before the desulfurization and dust removal device.The catalyst is easy to be deactivated by SO2and dust.In addition,the oxidation of Hg0 by commercial SCR catalyst is significantly influenced by the concentration of chlorine.Placing the SCR operation unit after the desulfurization and dust removal unit can alleviate SO2 poisoning considerably.However,it also reduced the temperature(below 200℃)of the gas entering the SCR operation unit.Therefore,the development of environmentally friendly catalysts with excellent NH3-SCR and Hg0 oxidation activity at low temperatures is crucial for the removal of NOx and Hg0 from flue gas simultaneously.Mn-based oxide catalysts have excellent low-temperature denitration activity,but their N2selectivity and sulfur resistance performance are poor.Ce-based oxides have excellent storage and release oxygen ability.Doping Ce into Mn-based oxides can tune their redox capacity,thereby improving the N2 selectivity and sulfur poisoning resistance of the catalysts.Ce-modified Mn-based catalysts lack systematic research on NO and Hg0 simultaneous removal,and the catalytic mechanism lacks in-depth research.In this thesis,the Ce-modified MnTiOxcatalyst was taken as the research object.Its Hg0 removal activity and its simultaneous NO and Hg0 removal activity were respectively studied.According to the characterization and analysis of catalysts,the removal mechanism of NOx and Hg0 on the catalyst was revealed.The main results and conclusions are as follows:(1)Ce-modified MnTiOx catalysts were prepared by PEG-assisted coprecipitation.The effects of reaction temperature and Ce content on the Hg0 removal activity of the catalysts were studied,and catalysts were characterized.With the increase of Ce content,the Hg0 removal efficiency of the catalysts first increases and then decreases.Among them,the Mn Ce(0.1)Ti Oxcatalyst exhibits the best Hg0 removal performance,and Hg0 removal efficiency beyond 95%at 100–300°C and 400,000 h-1.Characterization analysis results show after doping with Ce,the dispersibility of the catalyst metal oxides,the BET specific surface area,and thesurface-activee oxygen content are all improved,which are beneficial to the Hg0 removal of the catalyst.(2)Based on of the research on the Hg0 removal activity of the catalyst,taking the Mn Ce(0.1)Ti Ox catalyst as the research object,the influence of the gas composition on the Hg0removal activity of the catalyst was investigated,and the mechanism of Hg0 removal was revealed.NO and O2 are beneficial to the Hg0 removal,while NH3 inhibits the Hg0 removal.A low concentration of SO2 can promote the Hg0 removal;a high concentration of SO2 inhibits the Hg0 removal.The SCR reaction atmosphere inhibits Hg0 oxidation at high space velocity,which can be weakened by reducing the space velocity.Analysis using characterization shows that the Hg0 removal over Mn Ce Ti Ox catalyst follows the Mars–Maessen mechanism under N2+O2 atmosphere.(3)The performance of Ce-modified MnTiOx catalyst for simultaneous denitration and Hg0 removal was explored,and its mechanism for simultaneous denitration and mercury removal was revealed.With the increase of Ce content,the NO conversion and N2 selectivity of the catalyst gradually increased,and the Hg0 removal efficiency first increased and then decreased.Both SO2 and H2O will adversely affect the catalytic activity of the catalyst,the effect of SO2 is irreversible,and the effect of H2O is recoverable.The characterization and experimental results show that the denitration reaction over the Mn Ce Ti Ox catalyst follows the Langmuir–Hinshelwood mechanism and the Eley–Rideal mechanism,and the Langmuir–Hinshelwood mechanism is dominant;the Hg0 removal reaction follows the Mars–Maessen mechanism.
Keywords/Search Tags:Ce modified MnTiO_x catalyst, NO_x removal, Hg~0 oxidation, NH3 selective catalytic reduction, flue gas
PDF Full Text Request
Related items