Indexed by:期刊论文

First Author:Brown, S.

Correspondence Author:Brown, S (reprint author), UCL, Dept Chem Engn, London WC1E 7JE, England.

Co-author:Martynov, S.,Mahgerefteh, H.,Chen, S.,Zhang, Y.

Date of Publication:2014-11-01

Journal:INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL

Included Journals:SCIE、EI、Scopus

Document Type:J

Volume:30

Page Number:9-18

ISSN No.:1750-5836

Key Words:Multi-phase flow; CO2 pipeline safety; Mathematical modelling

Abstract:The development, testing and validation of a two-fluid transient flow model for simulating outflow following the failure of high pressure CO2 pipelines is presented. Thermal and mechanical non-equilibrium effects during depressurisation are accounted for by utilising simple constitutive relations describing inter-phase mass, heat and momentum transfer in terms of relaxation to equilibrium. Pipe wall/fluid heat exchange on the other hand is modelled by coupling the fluid model with a finite difference transient heat conduction model. The two-fluid transient flow model's performance is tested by comparison of the predicted transient pressure and temperature profiles along the pipeline against those based on the simplified homogeneous equilibrium model (HEM) as well as real data captured during the full bore rupture of a 260 m long, 233 mm internal diameter pipeline containing CO2 at 36 bara and 273 degrees C. The two-fluid model is found to produce a reasonably good degree of agreement with the experimental data throughout the depressurisation process. The HEM based flow model on the other hand performs well only near the rupture plane and during the early stages of the depressurisation process. (C) 2014 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY license (http://creativecommons.org/licenses/by/3.0/).

Translation or Not:no