Measurements of Decompression Wave Speed in Pure Carbon Dioxide and Comparison With Predictions by Equation of StateSource: Journal of Pressure Vessel Technology:;2016:;volume( 138 ):;issue: 003::page 31302DOI: 10.1115/1.4031941Publisher: The American Society of Mechanical Engineers (ASME)
Abstract: 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 largescale 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 lowlying 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 GERG2008, PengRobinson, and BWRS equations of state (EOS). These tests were conducted as a baseline before introducing various impurities.
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contributor author | Botros, K. K. | |
contributor author | Geerligs, J. | |
contributor author | Rothwell, B. | |
contributor author | Robinson, T. | |
date accessioned | 2017-05-09T01:32:44Z | |
date available | 2017-05-09T01:32:44Z | |
date issued | 2016 | |
identifier issn | 0094-9930 | |
identifier other | pvt_138_03_031302.pdf | |
identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/162353 | |
description abstract | 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 largescale 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 lowlying 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 GERG2008, PengRobinson, and BWRS equations of state (EOS). These tests were conducted as a baseline before introducing various impurities. | |
publisher | The American Society of Mechanical Engineers (ASME) | |
title | Measurements of Decompression Wave Speed in Pure Carbon Dioxide and Comparison With Predictions by Equation of State | |
type | Journal Paper | |
journal volume | 138 | |
journal issue | 3 | |
journal title | Journal of Pressure Vessel Technology | |
identifier doi | 10.1115/1.4031941 | |
journal fristpage | 31302 | |
journal lastpage | 31302 | |
identifier eissn | 1528-8978 | |
tree | Journal of Pressure Vessel Technology:;2016:;volume( 138 ):;issue: 003 | |
contenttype | Fulltext |