TY - JOUR
T1 - Depressurization of CO2 rich mixtures
T2 - Challenges for the safe process design of CCS facilities and CO2 EOR systems
AU - Luberti, Mauro
AU - Natarajan, Sathish
AU - Zaccheus, Yemi
AU - Giovanoglou, Apostolos
N1 - Publisher Copyright:
© Copyright 2016, AIDIC Servizi S.r.l.
PY - 2016
Y1 - 2016
N2 - The design of systems with high content of CO2 in the process mixture is of increasing importance. This is particularly true for emerging technologies such as Carbon Capture and Storage (CCS); with over twenty CCS installations worldwide (built or under-construction) and many more now progressing through front-end engineering & design and then to final investment decision. The design of the safety depressurization system for both CCS facilities and CO2 Enhanced Oil Recovery (EOR) installations is of particular importance, due to its impact on project costs. As with Oil & Gas processing facilities, the minimum metal temperatures in process equipment and piping are observed during highly transient depressurization operations ("blowdown"). The minimum metal temperature usually limits the material of construction: if metal temperatures below -46°C (-50°F) are possible then the usual requirement is to select materials that exhibit ductile behaviour below this point, typically stainless steel. Such choices have a huge impact on project costs, vessel order times and ultimately project viability. The design of the safety depressurization system for CO2 rich mixtures is difficult; CO2 introduces complex thermodynamic behaviour, for example: physical properties that are not accurately predicted by standard equation of state methods, a narrow phase envelope and the potential formation of solid phases during depressurization. Furthermore, physical plant configurations which are sectionalized for depressurization consist of multiple interconnected vessels and significant quantities of piping low points where condensate may accumulate. These locations are shown to be significant to depressuring temperatures. The design of such systems is not handled well using conventional depressurization methodologies; which rely on the representation of an actual plant segment as a single pseudo-vessel volume. In this paper, we present a validated methodology for analysing accurately the depressurization of high pressure gas processing facilities with rich CO2 mixtures. We describe the application of the methodology to the design of a CO2 EOR process.
AB - The design of systems with high content of CO2 in the process mixture is of increasing importance. This is particularly true for emerging technologies such as Carbon Capture and Storage (CCS); with over twenty CCS installations worldwide (built or under-construction) and many more now progressing through front-end engineering & design and then to final investment decision. The design of the safety depressurization system for both CCS facilities and CO2 Enhanced Oil Recovery (EOR) installations is of particular importance, due to its impact on project costs. As with Oil & Gas processing facilities, the minimum metal temperatures in process equipment and piping are observed during highly transient depressurization operations ("blowdown"). The minimum metal temperature usually limits the material of construction: if metal temperatures below -46°C (-50°F) are possible then the usual requirement is to select materials that exhibit ductile behaviour below this point, typically stainless steel. Such choices have a huge impact on project costs, vessel order times and ultimately project viability. The design of the safety depressurization system for CO2 rich mixtures is difficult; CO2 introduces complex thermodynamic behaviour, for example: physical properties that are not accurately predicted by standard equation of state methods, a narrow phase envelope and the potential formation of solid phases during depressurization. Furthermore, physical plant configurations which are sectionalized for depressurization consist of multiple interconnected vessels and significant quantities of piping low points where condensate may accumulate. These locations are shown to be significant to depressuring temperatures. The design of such systems is not handled well using conventional depressurization methodologies; which rely on the representation of an actual plant segment as a single pseudo-vessel volume. In this paper, we present a validated methodology for analysing accurately the depressurization of high pressure gas processing facilities with rich CO2 mixtures. We describe the application of the methodology to the design of a CO2 EOR process.
UR - http://www.scopus.com/inward/record.url?scp=84988699167&partnerID=8YFLogxK
U2 - 10.3303/CET1653061
DO - 10.3303/CET1653061
M3 - Article
AN - SCOPUS:84988699167
SN - 2283-9216
VL - 53
SP - 361
EP - 366
JO - Chemical Engineering Transactions
JF - Chemical Engineering Transactions
ER -