2014
DOI: 10.1016/j.egypro.2014.11.280
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Effect of Impurities on Depressurization of CO2 Pipeline Transport

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Cited by 16 publications
(8 citation statements)
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“…The releases were performed from approximately 120 bar and 20 • C and resulted in a coldest temperature of −35 • C for the CO 2 mixture containing 10 mole% nitrogen. Also other studies have investigated experimental depressurization of CO 2 pipelines, for the development (Håvelsrud, 2012) and testing (Huh et al, 2014) of multiphase flow simulator OLGA. It was found that the initial pressure drop was well simulated for both pure CO 2 and mixtures, but reliable temperature drop predictions were not provided (Huh et al, 2014).…”
Section: Introductionmentioning
confidence: 98%
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“…The releases were performed from approximately 120 bar and 20 • C and resulted in a coldest temperature of −35 • C for the CO 2 mixture containing 10 mole% nitrogen. Also other studies have investigated experimental depressurization of CO 2 pipelines, for the development (Håvelsrud, 2012) and testing (Huh et al, 2014) of multiphase flow simulator OLGA. It was found that the initial pressure drop was well simulated for both pure CO 2 and mixtures, but reliable temperature drop predictions were not provided (Huh et al, 2014).…”
Section: Introductionmentioning
confidence: 98%
“…Also other studies have investigated experimental depressurization of CO 2 pipelines, for the development (Håvelsrud, 2012) and testing (Huh et al, 2014) of multiphase flow simulator OLGA. It was found that the initial pressure drop was well simulated for both pure CO 2 and mixtures, but reliable temperature drop predictions were not provided (Huh et al, 2014). In an experimental investigation supported by Gassco , a 50 km long 24 in.…”
Section: Introductionmentioning
confidence: 98%
See 1 more Smart Citation
“…[24]. Huh et al [25] studied the severe pressure and temperature drops during the depressurization of dense CO2 in a 51.96 m long test tube with an inner diameter of 3.86 mm. The results of numerical simulations generated with OLGA were compared against experimental data.…”
Section: Introductionmentioning
confidence: 99%
“…The results of numerical simulations generated with OLGA were compared against experimental data. It was found that the initial pressure drop was well estimated by OLGA for both pure CO 2 and mixtures, but the numerical simulation did not provide reliable temperature drop predictions [25]. Clausen et al [26] described the results of depressurizing during CO 2 venting with an onshore 50 km long, 24 inch diameter buried pipeline from initially supercritical conditions.…”
Section: Introductionmentioning
confidence: 99%