2013
DOI: 10.1016/j.ijggc.2013.05.020
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A homogeneous relaxation flow model for the full bore rupture of dense phase CO2 pipelines

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Cited by 70 publications
(48 citation statements)
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“…that they move at the same velocity. In the HRM, the mass, momentum, energy and vapour quality conservation equations are respectively given by (Brown et al, 2013):…”
Section: Modelling Approachmentioning
confidence: 99%
See 1 more Smart Citation
“…that they move at the same velocity. In the HRM, the mass, momentum, energy and vapour quality conservation equations are respectively given by (Brown et al, 2013):…”
Section: Modelling Approachmentioning
confidence: 99%
“…Secondly, this solution is updated by solving a system of ordinary differential equations incorporating the expressions on the right-hand-side of equations (1) to (4). Full details of the algorithm are described in Brown et al (2013).…”
Section: Modelling Approachmentioning
confidence: 99%
“…Examples include study of cavitation in automotive fuel systems (Martynov et al, 2006), flash boiling of water during loss-of-coolant accidents in nuclear reactors (Nigmatulin and Soplenkov, 1994) and liquid boiling and expansion in refrigeration systems and heat pumps (Simões- Moreira and Bullard, 2003). In the particular context of Carbon Capture and Storage, the focus of such models has been on the flows resulting from pipeline decompression and failure (Brown et al, 2013b;Mahgerefteh et al, 2012;Munkejord et al, 2010).…”
Section: Introductionmentioning
confidence: 99%
“…no phase slip, is retained. However, non-equilibrium 214 liquid-vapour transition is accounted for by a relaxation to thermodynamic equilibrium following 215 Downar-Zapolski et al, (1996) and Brown et al, (2013). The choice of the time constant for the HRM 216 also follows that of Brown et al (2013).…”
mentioning
confidence: 99%
“…However, non-equilibrium 214 liquid-vapour transition is accounted for by a relaxation to thermodynamic equilibrium following 215 Downar-Zapolski et al, (1996) and Brown et al, (2013). The choice of the time constant for the HRM 216 also follows that of Brown et al (2013). Although the pressure is lower than the CO 2 triple point 217 pressure at the immediate vicinity of the release point, the framework assigned to Warwick team is the 218 atmospheric dispersion away from the three-phase, quickly expanding stages in the near proximity of 219 the release from the pipeline.…”
mentioning
confidence: 99%