SCI和EI收录∣中国化工学会会刊

中国化学工程学报 ›› 2021, Vol. 29 ›› Issue (1): 365-374.DOI: 10.1016/j.cjche.2020.08.045

• Energy Science and Technology • 上一篇    下一篇

Experimental and modeling study of the kinetics of methane hydrate formation and dissociation

Vafa Feyzi, Vahid Mohebbi   

  1. Ahvaz Petroleum Faculty, Petroleum University of Technology(PUT), Ahvaz, Iran
  • 收稿日期:2020-07-19 修回日期:2020-08-21 出版日期:2021-01-28 发布日期:2021-04-02
  • 通讯作者: Vafa Feyzi, Vahid Mohebbi

Experimental and modeling study of the kinetics of methane hydrate formation and dissociation

Vafa Feyzi, Vahid Mohebbi   

  1. Ahvaz Petroleum Faculty, Petroleum University of Technology(PUT), Ahvaz, Iran
  • Received:2020-07-19 Revised:2020-08-21 Online:2021-01-28 Published:2021-04-02
  • Contact: Vafa Feyzi, Vahid Mohebbi

摘要: In this work, several experiments were conducted at isobaric and isothermal condition in a CSTR reactor to study the kinetics of methane hydrate formation and dissociation. Experiments were performed at five temperatures and three pressure levels (corresponding to equilibrium pressure). Methane hydrate formation and dissociation rates were modeled using mass transfer limited kinetic models and mass transfer coefficients for both formation and dissociation were calculated. Comparison of results, shows that mass transfer coefficients for methane hydrate dissociation are one order greater than formation conditions. Mass transfer coefficients were correlated by polynomials as relations of pressure and temperature. The results and the method can be applied for prediction of methane production from naturally occurring methane hydrate deposits.

关键词: Methane hydrate, Kinetics, Formation, Dissociation, Mass transfer

Abstract: In this work, several experiments were conducted at isobaric and isothermal condition in a CSTR reactor to study the kinetics of methane hydrate formation and dissociation. Experiments were performed at five temperatures and three pressure levels (corresponding to equilibrium pressure). Methane hydrate formation and dissociation rates were modeled using mass transfer limited kinetic models and mass transfer coefficients for both formation and dissociation were calculated. Comparison of results, shows that mass transfer coefficients for methane hydrate dissociation are one order greater than formation conditions. Mass transfer coefficients were correlated by polynomials as relations of pressure and temperature. The results and the method can be applied for prediction of methane production from naturally occurring methane hydrate deposits.

Key words: Methane hydrate, Kinetics, Formation, Dissociation, Mass transfer