2012
DOI: 10.1002/ghg.1302
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A study of the effects of friction, heat transfer, and stream impurities on the decompression behavior in CO2 pipelines

Abstract: A transient multi‐phase outflow model is employed to study the effects of heat transfer and friction on the decompression behavior in CO2 pipelines. The model's predictions are compared to measurements obtained from a number of shock tube experiments for gaseous phase CO2 as well its various mixtures, typical of those found in the different capture technologies. Particular attention is paid to studying the impact of the stream impurities on the CO2 mixtures saturation pressures and the decompression wave speed… Show more

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Cited by 39 publications
(21 citation statements)
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“…Bishnoi [21,22], PipeTech [23,24] and CFD-DECOM [25]. These are based entirely on assumptions of one-dimensional homogeneous-equilibrium fluid flow.…”
Section: Computational Fluid Dynamics (Cfd) Technique Have Been Develmentioning
confidence: 99%
See 1 more Smart Citation
“…Bishnoi [21,22], PipeTech [23,24] and CFD-DECOM [25]. These are based entirely on assumptions of one-dimensional homogeneous-equilibrium fluid flow.…”
Section: Computational Fluid Dynamics (Cfd) Technique Have Been Develmentioning
confidence: 99%
“…These are based entirely on assumptions of one-dimensional homogeneous-equilibrium fluid flow. In these models the effects of friction, heat transfer, and pipe diameter can be considered, which is particularly relevant for smaller diameter and longer pipelines where friction could lead to a range of complex effects on local flow conditions, temperature, and pressure within the pipeline [24,[26][27][28][29]. CFD-based techniques involve discretising the governing partial differential equations of fluid flow.…”
Section: Computational Fluid Dynamics (Cfd) Technique Have Been Develmentioning
confidence: 99%
“…As noted by various 298 authors (Mahgerefteh et al, 2012b;Munkejord et al, 2010) this later behaviour is largely due to 299 frictional and heat transfer effects, the modelling of which is outside of this study. 300 Figure 8 shows the thermodynamic trajectory at the closed end of the pipeline section during the 301 decompression relative to the dew and bubble lines.…”
mentioning
confidence: 81%
“…36 ms. In contrast, the measured data fall steadily throughout this period, this is likely in part due 314 to the effects of friction and heat transfer which the fluid model applied here does not capture 315 accurately (Mahgerefteh et al, 2012b). Notably the measured pressure at P14 indicates a 316 subsequent acceleration of the pressure drop at the time predicted by the fluid model.…”
mentioning
confidence: 89%
“…A number of common cubic equations of state, e.g. the Soave-Redlich-Kwong (SRK) ( ) and the Peng-Robinson (PR) (Peng and Robinson, 1976) equations of state were employed for this purpose in modelling pipeline decompression (Mahgerefteh et al, 2012a;Mahgerefteh et al, 2012b;Munkejord et al, 2010 has been applied to predict outflow from pipelines with small diameter punctures. For modelling purposes, a pipeline with an orifice at the release end is considered as depicted in Figure 5.…”
Section: Modelling Approachmentioning
confidence: 99%