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Experimental And Mechanism Study On Simultaneous Removal Of SO2 And NOx Using Jet Bubble Reactor

Posted on:2010-09-03Degree:DoctorType:Dissertation
Country:ChinaCandidate:F LiuFull Text:PDF
GTID:1101360275984852Subject:Thermal Engineering
Abstract/Summary:PDF Full Text Request
The pollution status and removal technologies of SO2 and NOx were consulted andreviewed in this paper.NaClO2 were screened to be the absorbent of simultaneousdesulfurization and denitrification by experiments.Simulating coal-fired power plantconditions,experiments on removal of SO2 and NO by NaClO2 solution were carried outin a self-designed bubble reactor and a medium-scale CT-121 reactor.Based on theremoval products analysis and oxidation-reduction potential,the reaction and transfercharacteristic of the desulfurization and denitrification were revealed.The possibilityand limitation of the simultaneous desulfurization and denitrification using NaClO2 acidsolution were calculated and analyzed by chemical thermodynamic methods.Reactionkinetics of the simultaneous desulfurization and denitrification using NaClO2 solutionwere investigated by experiments.NaClO2 was determined to be the absorbent of the simultaneous desulfurization anddenitrification by screening experiments in a self-designed bubble reactor.Thecorresponding law and the optimal conditions were determined by the investigations ofthe effect of NaClO2 concentration,original pH value,reaction temperature,flue gasflow as wellas original concentration of SO2 and NO on the removal efficiencies.Underthe optimal conditions,the simultaneous removal efficiencies of SO2 and NO by NaClO2solution reached 100% and 95%,respectively.Based on the results of the packaged experiments and the practicle conditions ofcoal-fired power plants,the scale-up experiments on the simultaneous removal of SO2and NO by NaClO2 solutions were carried out in a medium-scale CT-121 reactor afterthe corresponding experimental parameters and the range were determined.Theexperimental results revealed the influence law of each parameter,and the optimalconditions were determined.Under the optimal conditions,the simultaneous removalefficeincies of SO2 and NO reached 82.0% and 92.8% above,respectively.The disproportion reactions of ClO2 in the NaClO2 solution were derived,and thepossibility,limitation and the predominant products of the reactions were analyzed bychemical thermodynamic methods.The conformational changes of chloride compoundsin NaClO2 solution were studied by experiments.The experimental results indicate thatthe main ion in the NaClO2 solution is ClO2- with a small amount of ClO2.The results of products analysis of the simultaneous desulfurization anddenitrification by NaClO2 solution show that sulfate radical ion is the predominantdesulfurization product,while nitrate radical ion is the predominant denitrification product.According to the products analysis and oxidation-reduction potential,thereaction processes of SO2 and NO in gas phase and liquid phase were investigated,respectively.And the total reaction equations of the desulfurization and denitrificationby NaClO2 acid solution were determined.The transfer characteristic of thedesulfurization and denitrification by NaClO2 solutionwasexplored by two-film theory.Molar reaction enthalpy,molar formation Gibbs function,SO2 and NO partialpressure at different reaction temperature as well as constant of reaction rate werecalculated and analyzed by chemical thermodynamic methods.The results show thatsimultaneous removal of SO2 and NO is feasibile in thermodynamic category.The reaction kinetic process of the simultaneous desulfurization and denitrificationby NaClO2 solution were investigated by experiments.The experimental results indicatethat the removal reaction of SO2 and NO are divided into two stages,as fast and slowreaction zone.Based on the experimental data,reaction partial order,macroscopy rateconstant and apparent activation energy of SO2 and NO were calculated.
Keywords/Search Tags:sodium chlorite, jet bubble reactor, simultaneous removal of SO2 and NO from flue gas, reaction kinetics
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