通过热重红外联用研究煤与污泥不同掺混比例样品的燃烧特性以及气体排放特性,分别利用Coats-Redfern模型和分布式活化能模型(distributed activation energy model,DAEM)对污泥与煤的掺烧过程进行动力学分析,研究2种模型的适用性。结果...通过热重红外联用研究煤与污泥不同掺混比例样品的燃烧特性以及气体排放特性,分别利用Coats-Redfern模型和分布式活化能模型(distributed activation energy model,DAEM)对污泥与煤的掺烧过程进行动力学分析,研究2种模型的适用性。结果表明,与单一煤样相比,10%掺混比例样品的着火点降低了11℃,可燃性能改善,稳燃性能提高,综合燃烧特性指数提高。此外,10%掺混比例样品燃烧过程中NO和SO 2的吸收峰比单一煤样的吸收峰低,说明一定比例掺混煤和污泥可以降低污染物的排放浓度。另外DAEM的拟合相关性系数比Coats-Redfern模型更高,表明DAEM更加适用于污泥与煤混合燃烧过程动力学分析。展开更多
The substitution of traditional blast furnaces with steel-belt furnaces for antimony smelting was proposed.The influence of various parameters on the oxidative volatilization of stibnite was studied according to the p...The substitution of traditional blast furnaces with steel-belt furnaces for antimony smelting was proposed.The influence of various parameters on the oxidative volatilization of stibnite was studied according to the production practice of steel-belt furnaces.Furthermore,the kinetics of oxidative volatilization was elucidated using differential thermal gravimetric analyses and non-isothermal analysis methods.The results indicated that the oxygen concentration and the temperature were pivotal variables in the oxidative volatilization process.Notably,the volatilization efficiency of antimony was 97.25%under optimal conditions.Moreover,the kinetic control stages were divided into chemical reaction control(440-490°C),internal diffusion control(500-550°C),and chemical reaction control(560-580°C).These stages corresponded to activation energies of 16.40-18.79,120.86-195.96,and 24.00-28.31 kJ/mol,respectively.展开更多
文摘通过热重红外联用研究煤与污泥不同掺混比例样品的燃烧特性以及气体排放特性,分别利用Coats-Redfern模型和分布式活化能模型(distributed activation energy model,DAEM)对污泥与煤的掺烧过程进行动力学分析,研究2种模型的适用性。结果表明,与单一煤样相比,10%掺混比例样品的着火点降低了11℃,可燃性能改善,稳燃性能提高,综合燃烧特性指数提高。此外,10%掺混比例样品燃烧过程中NO和SO 2的吸收峰比单一煤样的吸收峰低,说明一定比例掺混煤和污泥可以降低污染物的排放浓度。另外DAEM的拟合相关性系数比Coats-Redfern模型更高,表明DAEM更加适用于污泥与煤混合燃烧过程动力学分析。
基金supported financially by the National Natural Science Foundation of China(No.52074362)。
文摘The substitution of traditional blast furnaces with steel-belt furnaces for antimony smelting was proposed.The influence of various parameters on the oxidative volatilization of stibnite was studied according to the production practice of steel-belt furnaces.Furthermore,the kinetics of oxidative volatilization was elucidated using differential thermal gravimetric analyses and non-isothermal analysis methods.The results indicated that the oxygen concentration and the temperature were pivotal variables in the oxidative volatilization process.Notably,the volatilization efficiency of antimony was 97.25%under optimal conditions.Moreover,the kinetic control stages were divided into chemical reaction control(440-490°C),internal diffusion control(500-550°C),and chemical reaction control(560-580°C).These stages corresponded to activation energies of 16.40-18.79,120.86-195.96,and 24.00-28.31 kJ/mol,respectively.
