Adsorption isotherms and kinetics of carbon dioxide on Chinese dry coal over a wide pressure range

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• 作者：Yongchen Song ; Wanli Xing ; Yi Zhang ; Weiwei Jian ; Zhaoyan Liu ; Shuyang Liu
• 关键词：Adsorption isotherms ; Thermodynamic model ; Kinetics ; Diffusivity
• 刊名：Adsorption
• 出版年：2015
• 出版时间：February 2015
• 年：2015
• 卷：21
• 期：1-2
• 页码：53-65
• 全文大小：630 KB
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• 作者单位：Yongchen Song (1)
  Wanli Xing (1)
  Yi Zhang (1)
  Weiwei Jian (1)
  Zhaoyan Liu (1)
  Shuyang Liu (1)
  
  1. Key Laboratory of Ocean Energy Utilization and Energy Conservation of Ministry of Education, School of Energy and Power Engineering, Dalian University of Technology, Dalian, 116024, People’s Republic of China
  
• 刊物类别：Chemistry and Materials Science
• 刊物主题：Chemistry
  Surfaces and Interfaces and Thin Films
  Industrial Chemistry and Chemical Engineering
  Engineering Thermodynamics and Transport Phenomena
  
• 出版者：Springer Netherlands
• ISSN：1572-8757

文摘

A gravimetric method with in situ density measurement is used to determine the adsorption isotherms and kinetic characteristics of CO2 on Chinese dry coal plug at 293.29, 311.11, 332.79 and 352.57?K and pressures up to 19?MPa. The adsorption and desorption process is reversible, which shows that it is a process of physical adsorption for CO2 on coal. The excess adsorption increases with the increasing pressure at low pressures until the CO2 phase transitions pressure is reached. Above this pressure, the excess adsorption decreases with the increasing pressure. The adsorption behaviour is described using the CO2 density instead of pressure in four thermodynamic models such as modified Langmuir, Langmuir?+?k, DR and DR?+?k. It is found that the modified Langmuir?+?k and DR?+?k models are more suitable for liquid and supercritical CO2 adsorption, respectively. The adsorption kinetics data are also obtained during the measurement of adsorption isotherms. The experimental data are fluctuant at the initial time range due to the temperature variation in the adsorption cell after high-pressure CO2 is injected. The diffusivity is estimated using a modified unipore model. It is observed that the kinetic parameter C, accounting for the effect of gas diffusivity, increases with the increasing pressure at low pressures and has no obvious relations with pressure at high pressures. In this study, C value has no dependencies with temperature for CO2, and the order of magnitude of the effective diffusivity is approximately 10? to 10??s?.