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Transformation Behaviors Of MoO3 As Gaseous Oxygen Carrier And Reaction Characteristics Of Coal In Chemical Looping Gasification

Posted on:2020-07-18Degree:MasterType:Thesis
Country:ChinaCandidate:J X KangFull Text:PDF
GTID:2381330596985886Subject:Chemical Engineering and Technology
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Conventional coal gasification technologies are often suffered with parasitic energy penalty and additional capital expenses because of oxygen separation preparation,which also caused an amount of CO2 emissions.Chemical-looping gasification?CLG?of coal to yield syngas is a clean and effective coal gasification technology which can realize the cascade utilization of energy and avoid the use of air separation unit due to lattice oxygen replaces the oxygen,therefore,CLG has the potential to reduce CO2.In this study,a novel concept of coal gasification using chemical-looping technology with molybdenum trioxide?MoO3?as a gaseous oxygen carrier?CLG?was proposed.MoO3 as an oxygen carrier has potential to increase the reaction rate of coal and MoO3,as well as to reduce the difficulty of oxygen carrier-ash separation in the CLG process due to MoO3's volatility.In this study,thermodynamic analysis of the reaction between coal and MoO3 were investigated by HSC Chemistry 6.0 based on the Gibbs free energy minimization principle.The effects of key parameters such as the mass ratio of MoO3/C?R?and temperature on the transformation behavior of MoO3 were investigated in a fixed bed reactor.In addition,the effects of the above key parameters on the gasification reactivity of different degree of coalification coal in complex atmosphere were also investigated.At last,the hydrogen production capacity and cyclic stability of MoO3 were studied.The main results and conclusions are as follows:1.MoO3 can be used as an oxygen carrier in chemical looping gasification?CLG?by analyzing the Ellingham diagram.According to the comparison of thermodynamic parameters of the reactions that the system may be involved,MoO3 had an excellent oxidization ability to carbon than to syngas,so MoO3 was more suitable for chemical looping gasification?CLG?.2.The key parameters of the mass ratio of MoO3 to graphite?R?and the temperature had an important influence on the transformation behavior of MoO3.When T>1273 K,Mo was generated,when T<1273 K,MoO2 were the main products.In order to save the amount of MoO3,the temperature should keep at higher 1273 K.When MoO3 was insufficient?R<5?,the side reaction2Mo+C?Mo2 C will happen which can lead to ineffective carbon conversion.When R=5,it was suitable for carbon conversion,no side reactions occur.When MoO3 was excess?R>5?,the side reaction2MoO3+Mo?3MoO2 will occur which can lead to ineffective MoO3 conversion.In order to avoid side reactions,R=5 was suitable.3.The carbon conversion efficiency of gas coal,fat coal and coke coal were46.80%,33.91%and 29.54%respectively in absence of H2O.With the increase of F,the effective carbon conversion increases gradually and the carbon conversion efficiency increased to 55.00%,46.40%and 40.00%when sufficient H2O was added.Therefore,the reactivity of the three kinds of bituminous coals were successively:gas coal>fat coal>coke coal,which was positively correlated with the volatile content.4.By analyzing the evolution of H2 in CLG process,it was concluded that the main reasons for the change of H2 were as follows:Mo+2H 2O?MoO2+2H2.Based on the above analysis,the hydrogen production capacity and cycling performance of MoO3 oxygen carriers were also investigated,and it was found that the water conversion efficiency could reach94.84%at 1373 K.Through the study of cyclic properties,it was found that there was no sintering phenomenon of MoO3 oxygen carrier and it had excellent cyclic stability.
Keywords/Search Tags:chemical looping gasification, coal, MoO3 oxygen carrier, transformation behavior, reaction characteristic
PDF Full Text Request
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