SO2对钾基吸附剂CO2吸附性能的影响及机理研究

Mechanism study on the effect of SO2 on CO2 adsorption performance of potassium-based adsorbent

  • 摘要: 燃煤电厂尾部烟气经脱硫后,存在的痕量SO2会导致钾基吸附剂CO2吸附性能恶化。以结晶氯化铝为前驱体,采用溶胶-凝胶法制备K2CO3/Al2O3固体吸附剂,利用固定床反应系统,模拟烟气组分,在含SO2(0、150、250、400 mg/m3)气氛下的CO2吸附特性进行了吸附实验,结合BET、XRD表征手段,分析吸附剂孔隙结构和物质组成,采用DFT理论研究了SO2对K2CO3/Al2O3(0001)吸附剂表面吸附CO2的影响及机理。结果表明,在理想气氛中,钾基吸附剂CO2累积吸附量为1.72 mmol/g,当反应气氛中存在150 mg/m3 SO2时,钾基吸附剂与SO2发生反应生成K2SO3,导致吸附剂的吸附量(1.38 mmol/g)降低了19.77%,SO2质量浓度增至400 mg/m3,钾基吸附剂CO2累积吸附量逐渐降至1.26 mmol/g,吸附剂吸附CO2性能恶化,钾基吸附剂在7次循环后吸附量降为1.1 mmol/g,循环性能变差。CO2、SO2两种分子在K2CO3/Al2O3(0001)表面吸附位点均为Al-O桥位,H2O分子的吸附位点为O顶位。K2CO3/Al2O3(0001)表面对SO2的吸附作用大于H2O和CO2。H2O和CO2共吸附时CO2分子中O-s轨道与H-s轨道重叠,使得2者在表面吸附时可以相互促进;SO2分子由于其S、O原子p轨道活跃,与CO2共吸附时,会优先抢占CO2的吸附位点,抑制CO2在表面的吸附。H2O分子对K2CO3/Al2O3(0001)表面吸附SO2的促进作用大于CO2,H2O的存在会加速SO2与表面的反应,导致吸附剂表面对CO2吸附能力变差。CO2与H2O共吸附于K2CO3/Al2O3(0001)表面时碳酸化反应机理为H2O分子中H+和OH,分别与\mathrmCO_3^2- 和CO2形成\mathrmHCO_3^- ,反应能垒为1.12 eV,反应热为−1.47 eV。

     

    Abstract: After desulphurization, the trace amount of SO2 in the tail gas of coal-fired power plant will lead to the deterioration of CO2 adsorption performance of potassium-based adsorbent. Using crystalline aluminum chloride as precursor, the solid adsorbent K2CO3/Al2O3 was prepared by sol-gel method. The adsorption characteristics of CO2 in SO2 (0, 150, 250 and 400 mg/m3) atmosphere were simulated by fixed bed reaction system. Combined with the BET and XRD characterization methods, the pore structure and material composition of the adsorbent were analyzed. The influence of SO2 on the surface adsorption of CO2 by K2CO3/Al2O3(0001) was studied by using the DFT theory. The results showed that in the ideal atmosphere, the cumulative adsorption capacity of CO2 of potassium adsorbent is 1.72 mmol/g. In the presence of 150 mg/m3 SO2 in the reaction atmosphere, the potassium adsorbent reacts with SO2 to form K2SO3, resulting in a 19.77% decrease in adsorption capacity (1.38 mmol/g). When the concentration of SO2 increases to 400 mg/m3, the cumulative adsorption capacity of CO2 of potassium-based adsorbent gradually decreases to 1.26 mmol/g, the adsorption performance of CO2 of the adsorbent is deteriorated. The adsorption capacity of potassium-based adsorbent decreases to 1.1 mmol/g after seven cycles, and the cycle performance is deteriorated. The adsorption sites of CO2 and SO2 on the surface of K2CO3/Al2O3(0001) are Al-O bridge sites, and the H2O molecules are O top sites. The adsorption of SO2 on K2CO3/Al2O3(0001) surface is greater than that on H2O and CO2. When H2O and CO2 are co-adsorbed, the O-s orbitals and H-s orbitals overlap in the CO2 molecules, so that the two can promote each other during surface adsorption. Due to the active p orbitals of S and O atoms, the SO2 molecules preferentially preempt the adsorption site of CO2 and inhibit the adsorption of CO2 on the surface when co-adsorbed with CO2. The catalytic effect of H2O molecules on the adsorption of SO2 on the surface of K2CO3/Al2O3(0001) is greater than that of CO2. The presence of H2O will accelerate the reaction between SO2 and the surface, leading to the deterioration of the adsorption capacity of CO2 on the surface of the adsorbent. When CO2 and H2O are co-adsorbed on K2CO3/Al2O3(0001) surface, the carbonation mechanism is H+ and OH in H2O molecules, which forms \mathrmHCO_3^- with \mathrmCO_3^2- and CO2 respectively. The reaction energy barrier is 1.12 eV, and the reaction heat is −1.47 eV.

     

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