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Mathematical Model and Numerical Analysis for Packed Bed Methanation Reactors

충전층 메탄화 반응기의 수학적 모델 및 전산 수치해석

  • Received : 2015.05.27
  • Accepted : 2015.06.30
  • Published : 2015.06.30

Abstract

One-dimensional packed bed reactor model accounting for interfacial and intra-particle gradients was developed and based on it numerical analyses were performed to investigate the dynamic behavior of a commercial scale methanation reactor. Methanation reaction was almost complete near the reactor inlet and gases with equilibrated composition were discharged from the reactor. Both the intra-particle temperature gradient and differential surface temperature rise were found to be severe near the reactor inlet. To reduce the possible degradation or fracture of catalyst particles and prevent local overheating on the catalyst, addition of inert material can be an effective way.

Keywords

References

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