| Calcium looping is one of the most promising carbon capture technology for coal-fired power plants,due to its advantages of high capture efficiency,wide source of raw materials and low economic cost.However,the combined effect of H2O and SO2 in coal flue gas on CO2 capture by calcium looping is not clear,which limits the application of calcium looping in actual coal flue gas conditions.Therefore,the thermostatic thermogravimetric system was used to systematically study the combined effect of H2O and SO2 on CO2 capture in calcium looping,and characterization of nitrogen adsorption and morphology were employed to further explore the mechanism of H2O and SO2.Finally,considering the combined effects of H2O and SO2,the random pore reaction model of calcium cycle was established.It is expected to provide theoretical support for the development of calcium looping technology.The research results are as follows:(1)The independent influence mechanism of H2O and SO2 on calcium looping in carbonation atmosphere was proved.In the carbonation stage,H2O improves the adsorbent pore structure and reduces the diffusion resistance of CO2 in the CaO particle pore,accelerating the carbonation rate in the rapid reaction stage.Thus,H2O improves the carbonation conversion rate.For example,when the carbonation stage contains 20%H2O,the carbonation conversion rate in the 10th cycle increases by 4.41%compared with the condition without H2O.When SO2 acts alone,SO2 and CO2 compete for CaO reaction sites.And Ca SO4 blocks particle pores and hinders the diffusion of CO2,therefore reducing the carbonation conversion rate.In addition,the hindering effect becomes more obvious with the increase of cycle number.(2)The combined effect and mechanism of H2O and SO2 on calcium looping in carbonation atmosphere were proved.When the carbonation atmosphere contains10%H2O,the pore clogging of absorbent becomes more serious with the increase of SO2 concentration from 0%to 0.1%,resulting in a decrease in the ability of circulating CO2 capture.When the carbonation atmosphere contains 0.05%-0.1%SO2,the absorbent pore volume increases gradually with the increase of H2O concentration from 0%to 20%,the large pores increase significantly,and the carbon capture capacity is improved.The combined effect of H2O and SO2 is reflected in the fact that H2O weakens the blocking effect of SO2 on CO2 capture and improves the carbonation conversion rate of absorbent.(3)Considering the sintering of CaO particles,the effect of H2O and the simultaneous carbonation/sulfuration reaction,the random pore model of calcination,carbonation and sulfuration reaction of calcium based adsorbent was established.The reaction model can accurately describe the chemical reaction processes such as calcination,carbonation and sulfuration.The calculation results show that the outer layer of the adsorbent particles has a higher conversion rate,while the closer it is to the inside of the particles,the lower the conversion rate.In addtion,the conversion difference between the inner and outer layer of the adsorbent particles increases with the reaction time.H2O improves the local carbonation conversion rate of the inner and outer layers of particles,while SO2reduces the local carbonation conversion rate of particles.At the same time,CaO still maintains a high local carbonation conversion rate under the synergism of H2O and SO2. |