SCI和EI收录∣中国化工学会会刊

›› 2010, Vol. 18 ›› Issue (2): 223-230.

• SEPARATION SCIENCE AND ENGINEERING • Previous Articles     Next Articles

An Adsorption Kinetic Model for Sulfur Dioxide Adsorption by ZL50 Activated Carbon

GAO Jixian, WANG Tiefeng, SHU Qing, Zeeshan Nawaz, WEN Qian, WANG Dezheng, WANG Jinfu Beijing   

  1. Key Laboratory of Green Chemical Reaction Engineering and Technology, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
  • Received:2009-06-18 Revised:2010-01-07 Online:2010-04-28 Published:2010-04-28

An Adsorption Kinetic Model for Sulfur Dioxide Adsorption by ZL50 Activated Carbon

高继贤, 王铁峰, 舒庆, 山尼, 温倩, 王德峥, 王金福   

  1. Key Laboratory of Green Chemical Reaction Engineering and Technology, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
  • 通讯作者: WANG Jinfu,E-mail:wangjf@flotu.org

Abstract: A semi-empirical adsorption kinetic model was proposed with the time compensation method to describe the chemisorption of SO2 in flue gas by carbon adsorbents for flue gas purification.The change in adsorption capacity and adsorption rate with time at different water vapor concentrations and different SO2 concentrations was studied.The model was in good agreement with experimental data.The surface reaction was probably the rate controlling step in the early stage for SO2 adsorption by ZL50 activated carbon.The parameters m and n in the nth order adsorption kinetic model were related to the magnitude of the time compensation and adsorption driving force,respectively.The change of parameter n with water vapor concentrations and sulfur dioxide concentrations was studied and some physical implications were given.The sum of square errors was less than 1.0 and the average absolute percentage deviations ranged from 0.5 to 3.2.The kinetic model was compared with other models in the literature.

Key words: adsorption kinetic model, time compensation method, flue gas purification, ZL50 activated carbon, adsorption capacity, adsorption rate

摘要: A semi-empirical adsorption kinetic model was proposed with the time compensation method to describe the chemisorption of SO2 in flue gas by carbon adsorbents for flue gas purification.The change in adsorption capacity and adsorption rate with time at different water vapor concentrations and different SO2 concentrations was studied.The model was in good agreement with experimental data.The surface reaction was probably the rate controlling step in the early stage for SO2 adsorption by ZL50 activated carbon.The parameters m and n in the nth order adsorption kinetic model were related to the magnitude of the time compensation and adsorption driving force,respectively.The change of parameter n with water vapor concentrations and sulfur dioxide concentrations was studied and some physical implications were given.The sum of square errors was less than 1.0 and the average absolute percentage deviations ranged from 0.5 to 3.2.The kinetic model was compared with other models in the literature.

关键词: adsorption kinetic model, time compensation method, flue gas purification, ZL50 activated carbon, adsorption capacity, adsorption rate