Depressurization of CO2-N2 and CO2-He in a pipe: Experiments and modelling of pressure and temperature dynamics

被引:14
作者
Munkejord, Svend Tollak [1 ]
Deng, Han [1 ]
Austegard, Anders [1 ]
Hammer, Morten [1 ]
Aasen, Ailo [1 ]
Skarsvag, Hans L. [1 ]
机构
[1] SINTEF Energy Res, POB 4761, NO-7034 Trondheim, Norway
关键词
Carbon dioxide; Depressurization; Decompression; Experiment; Impurities; Thermodynamics; Fluid dynamics; EQUATION-OF-STATE; CARBON-DIOXIDE; 2-PHASE FLOW; TRANSPORT-PROPERTIES; SUPERCRITICAL CO2; STREAM IMPURITIES; CUBIC EQUATIONS; HEAT-TRANSFER; DECOMPRESSION; PIPELINES;
D O I
10.1016/j.ijggc.2021.103361
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
To design and operate safe and efficient CO2-transportation systems for CO2 capture and storage (CCS), engineers need simulation tools properly accounting for the fluid and thermodynamics of CO2. As the transportation systems evolve into networks, it becomes important that these tools also account for impurities in the CO2, which may significantly affect the thermophysical properties, directly impacting system design and safety. Tube depressurization experiments provide crucial data to develop and validate models describing transient multi-phase multicomponent flow in pipes. In this work, we perform experiments in a new facility with dense and fast instrumentation for both pressure and temperature. One experiment is for CO2 with 1.8 mol % N-2, and one has 1.92 mol % He, both starting from 12 MPa and 25 degrees C. In order to quantify the effect of impurities, the experiments are compared to results for pure CO2 and analysed on the background of simulations. We employ a homogeneous equilibrium model (HEM) augmented in this work to account for the appearance of solid CO2 in CO2 mixtures. We observe that the moderate amounts of impurities significantly influence both pressure and temperature dynamics. In particular, the 'pressure plateau', a key quantity for the assessment of running-ductile fracture, increases as much as 4 MPa for CO2-He compared to pure CO2. A further insight is that models must account for solid CO2 in order to capture the correct temperature development as the pressure decreases towards atmospheric conditions.
引用
收藏
页数:16
相关论文
共 68 条
[31]  
GUNGOR KE, 1987, CHEM ENG RES DES, V65, P148
[32]   Pressure responses and phase transitions during the release of high pressure CO2 from a large-scale pipeline [J].
Guo, Xiaolu ;
Yan, Xingqing ;
Yu, Jianliang ;
Yang, Yang ;
Zhang, Yongchun ;
Chen, Shaoyun ;
Mahgerefteh, Haroun ;
Martynov, Sergey ;
Collard, Alexander .
ENERGY, 2017, 118 :1066-1078
[33]   Pressure response and phase transition in supercritical CO2 releases from a large-scale pipeline [J].
Guo, Xiaolu ;
Yan, Xingqing ;
Yu, Jianliang ;
Zhang, Yongchun ;
Chen, Shaoyun ;
Mahgerefteh, Haroun ;
Martynov, Sergey ;
Collard, Alexander ;
Proust, Christophe .
APPLIED ENERGY, 2016, 178 :189-197
[34]  
Hammer M., 2020, THERMOPACK
[35]   Method Using a Density-Energy State Function with a Reference Equation of State for Fluid-Dynamics Simulation of Vapor-Liquid-Solid Carbon Dioxide [J].
Hammer, Morten ;
Ervik, Asmund ;
Munkejord, Svend Tollak .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (29) :9965-9978
[36]   Effect of Impurities on Depressurization of CO2 Pipeline Transport [J].
Huh, Cheol ;
Cho, Meang-Ik ;
Hong, Sup ;
Kang, Seong-Gil .
12TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-12, 2014, 63 :2583-2588
[37]  
IPCC, 2018, SPEC REP GLOB WARM 1, DOI DOI 10.1017/9781009157926.005
[38]   Equation of State for Solid Carbon Dioxide Based on the Gibbs Free Energy [J].
Jaeger, Andreas ;
Span, Roland .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2012, 57 (02) :590-597
[39]  
Jie HE, 2013, PROCEEDINGS OF THE 9TH INTERNATIONAL PIPELINE CONFERENCE - 2012, VOL 3, P585
[40]  
Jones D.G., 2013, 6 INT PIP TECHN C LA