Carbon dioxide capture and storage (CCS) is one of the technologies that have been proposed to reduce emissions of carbon dioxide (CO2) to the atmosphere. CCS will require the transportation of the CO2 from the “capture” locations to the “storage” locations via large-scale pipeline projects. One of the key requirements for the design and operation of pipelines in all jurisdictions is fracture control. Supercritical CO2 is a particularly challenging fluid from this point of view, because its thermodynamic characteristics are such that a very high driving force for fracture can be sustained for a long time. Even though CO2 is not flammable, it is an asphyxiating gas that is denser than air, and can collect in low-lying areas. Additionally, it is well known that any pipeline rupture, regardless of the nature of the fluid it is transporting, has a damaging reputational, commercial, logistic, and end user impact. Therefore, it is as important to control fracture in a CO2 pipeline as in one transporting a flammable fluid. With materials specified appropriately for the prevention of brittle failure, the key element is the control of propagating ductile (or tearing) fracture. The determination of the required toughness for the arrest of ductile fracture requires knowledge of the decompression behavior of the contained fluid, which in turn requires accurate knowledge of its thermodynamic characteristics along the decompression isentrope. While thermodynamic models based on appropriate EOS (equations of state) are available that will, in principle, allow determination of the decompression wave speed, they, in general, have not been fully validated for very rapid transients following a rupture. This paper presents experimental results of the decompression wave speed obtained from shock tube tests conducted on pure CO2 from different initial conditions, and comparison with predictions by models based on GERG-2008, Peng-Robinson, and BWRS equations of state (EOS). These tests were conducted as a baseline before introducing various impurities.
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June 2016
Research-Article
Measurements of Decompression Wave Speed in Pure Carbon Dioxide and Comparison With Predictions by Equation of State
J. Geerligs,
J. Geerligs
NOVA Chemicals Centre for Applied Research,
Calgary, AB T2E 7K7, Canada
Calgary, AB T2E 7K7, Canada
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B. Rothwell,
B. Rothwell
Brian Rothwell Consulting Inc.,
Calgary, AB T3A 5V9, Canada
Calgary, AB T3A 5V9, Canada
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T. Robinson
T. Robinson
TransCanada PipeLines Limited,
Calgary, AB T2P 5H1, Canada
Calgary, AB T2P 5H1, Canada
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K. K. Botros
J. Geerligs
NOVA Chemicals Centre for Applied Research,
Calgary, AB T2E 7K7, Canada
Calgary, AB T2E 7K7, Canada
B. Rothwell
Brian Rothwell Consulting Inc.,
Calgary, AB T3A 5V9, Canada
Calgary, AB T3A 5V9, Canada
T. Robinson
TransCanada PipeLines Limited,
Calgary, AB T2P 5H1, Canada
Calgary, AB T2P 5H1, Canada
1Corresponding author.
Contributed by the Pressure Vessel and Piping Division of ASME for publication in the JOURNAL OF PRESSURE VESSEL TECHNOLOGY. Manuscript received May 27, 2015; final manuscript received October 22, 2015; published online December 10, 2015. Assoc. Editor: Chong-Shien Tsai.
J. Pressure Vessel Technol. Jun 2016, 138(3): 031302 (8 pages)
Published Online: December 10, 2015
Article history
Received:
May 27, 2015
Revised:
October 22, 2015
Citation
Botros, K. K., Geerligs, J., Rothwell, B., and Robinson, T. (December 10, 2015). "Measurements of Decompression Wave Speed in Pure Carbon Dioxide and Comparison With Predictions by Equation of State." ASME. J. Pressure Vessel Technol. June 2016; 138(3): 031302. https://doi.org/10.1115/1.4031941
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