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.

References

1.
IPCC Special Report on Carbon Dioxide Capture and Storage
,
Metz
,
B.
,
Davidson
,
O.
,
de Coninck
,
H.
,
Loos
,
M.
, and
Meyer
,
L.
,
2005
, Intergovernmental Panel on Climate Change,
Cambridge University Press
,
Cambridge, MA
.
2.
Gale
,
J.
, and
Davidson
,
J.
,
2004
, “
Transmission of CO2—Safety and Economic Considerations
,”
Energy
,
29
(
9–10
), pp.
1319
1328
.
3.
Cosham
,
A.
,
Eiber
,
R. J.
, and
Clark
,
E. B.
,
2010
, “
GASDECOM: Carbon Dioxide and Other Components
,”
8th International Pipeline Conference
,
Calgary, AB, Canada
, Sept. 27–Oct. 1, Paper No. IPC 2010-31572.
4.
Cosham
,
A.
, and
Eiber
,
R. J.
,
2008
, “
Fracture Control in Carbon Dioxide Pipelines—The Effect of Impurities
,”
7th International Pipeline Conference
, Calgary, AB, Canada, Sept. 29–Oct. 3, Paper No. IPC 2008-64346.
5.
Seevam
,
P. N.
,
Race
,
J. M.
,
Downie
,
M. J.
, and
Hopkins
,
P.
,
2008
, “
Transporting the Next Generation of CO2 for Carbon, Capture and Storage: The Impact of Impurities on Supercritical CO2 Pipelines
,”
7th International Pipeline Conference
,
Calgary, AB, Canada
, Sept. 29–Oct. 3, Paper No. IPC2008-64063.
6.
Nahas
,
G.
, and
Mohitpour
,
M.
,
2010
, “
Engineering Pipelines for Transportation of CO2 With Impurities
,”
8th International Pipeline Conference
,
Calgary, AB, Canada
, Sept. 27–Oct. 1, Paper No. IPC 2010-31651.
7.
Eiber
,
R. J.
,
Bubenik
,
T. A.
, and
Maxey
,
W. A.
,
1993
, “
Fracture Control Technology for Natural Gas Pipelines
,” Pipeline Research Council International, Falls Church, VA, PRCI Catalogue No. L51691.
8.
Eiber
,
R. J.
,
Carlson
,
L.
, and
Leis
,
B.
,
2004
, “
Fracture Control Requirements for Gas Transmission Pipelines
,”
4th International Conference on Pipeline Technology
,
Ostend, Belgium, May 9–13, Scientific Surveys
,
Beaconsfield, UK
, pp.
437
446
.
9.
Eiber
,
R. J.
, and
Maxey
,
W. A.
,
1977
, “
Full-Scale Experimental Investigation of Ductile Fracture Behaviour in Simulated Arctic Pipeline
,”
Materials Engineering in the Arctic
,
ASM
,
Metals Park, OH
, p.
306
.
10.
Maxey
,
W. A.
,
Kiefner
,
J. C.
,
Eiber
,
R. J.
, and
Duffy
,
A. R.
,
1972
, “
Ductile Fracture Initiation, Propagation and Arrest in Cylindrical Vessels
,” Fracture Toughness, 1971 National Symposium on Fracture Mechanics, Urbana-Champaign, IL, Aug. 31–Sept. 2, American Society for Testing and Materials, Philadelphia, PA, Report No.
ASTM STP
514, pp.
70
81
.
11.
Maxey
,
W. A.
,
1974
, “
Fracture Initiation, Propagation and Arrest
,”
5th Symposium on Line Pipe Research
, Houston, TX, Nov. 20–22, Pipeline Research Council International, Falls Church, VA, PRCI Catalogue No. L30174.
12.
Rothwell
,
A. B.
,
1997
, “
Fracture Propagation Control Measures for Gas Pipelines
,”
International Seminar on Fracture Control in Gas Pipelines
, Sydney, June 3,
WTIA
,
Sydney, Australia
, pp.
6-1
6-14
.
13.
Elshahomi
,
A.
,
Lu
,
C.
,
Michal
,
G.
,
Liu
,
X.
,
Godbole
,
A.
, and
Venton
,
P.
,
2015
, “
Decompression Wave Speed in CO2 Mixtures: CFD Modelling With the GERG-2008 Equation of State
,”
Appl. Energy
,
140
, pp.
20
32
.
14.
Botros
,
K. K.
,
Craidy
,
P.
, and
Hippert
,
E.
, Jr.
,
2013
, “
Measurements of Decompression Wave Speed in Mixtures of Carbon Dioxide and Methane Using Specialized Shock Tube
,”
Rio Pipeline Conference & Exposition 2013
,
Rio de Janeiro, Brazil
, Sept. 22–24, Paper No. IBP1497_13.
15.
Botros
,
K. K.
,
Hippert
,
E.
, Jr.
, and
Craidy
,
P.
,
2013
, “
Measuring Decompression Wave Speed in CO2 Mixtures by a Shock Tube
,”
Int. Pipelines Mag.
,
16
(
June
), pp.
22
26
.
16.
Munkejord
,
S. T.
, and
Hammer
,
H.
,
2015
, “
Depressurization of CO2-Rich Mixtures in Pipes: Two-Phase Flow Modelling and Comparison With Experiments
,”
Int. J. Greenhouse Gas Control
,
37
, pp.
398
411
.
17.
Cosham
,
A.
,
Jones
,
D. G.
,
Armstrong
,
K.
,
Allason
,
D.
, and
Barnett
,
J.
,
2012
, “
The Decompression Behaviour of Carbon Dioxide in the Dense Phase
,”
ASME
Paper No. IPC2012-90461.
18.
Botros
,
K. K.
,
Geerligs
,
J.
,
Rothwell
,
B.
,
Buterbaugh
,
C.
,
Hsiao
,
C. P.
,
Venton
,
P.
,
Cooper
,
R.
, and
Robinson
,
T.
,
2013
, “
Shock Tube Measurements of Decompression Wave Speed in CO2 With Impurities
,” Pipeline Research Council International, Falls Church, VA, PRCI Report No. PR#383-104506.
19.
Botros
,
K. K.
,
Geerligs
,
J.
, and
Eiber
,
R. J.
,
2010
, “
Measurement of Decompression Wave Speeds in Rich Gas Mixtures at High Pressures (370 Bar) Using Specialized Rupture Tube
,”
ASME J. Pressure Vessel Technol.
,
132
(
5
), p.
051303
.
20.
Botros
,
K. K.
,
Geerligs
,
J.
,
Rothwell
,
B.
,
Carlson
,
L.
,
Fletcher
,
L.
, and
Venton
,
P.
,
2010
, “
Transferability of Decompression Wave Speed Measured by a Small Diameter Shock Tube to Full Size Pipelines and Implication for Determining Required Fracture Propagation Resistance
,”
Int. J. Pressure Vessel Piping
,
87
(
12
), pp.
681
695
.
21.
Botros
,
K. K.
,
Geerligs
,
Carlson
,
L.
, and
Reed
,
M.
,
2013
, “
Experimental Validation of GASDECOM for Ultra-Rich (58 MJ/m3) Natural Gas Mixtures by Specialized Shock Tube
,”
Int. J. Pressure Vessel Piping
,
107
, pp.
20
26
.
22.
Botros
,
K. K.
,
Geerligs
,
J.
,
Rothwell
,
B.
, and
Robinson
,
T.
, “
Measurements of Decompression Wave Speed in Binary Mixtures of Carbon Dioxide and Impurities
,”
ASME J. Pressure Vessel Technol.
(submitted).
23.
Botros
,
K. K.
,
Geerligs
,
J.
,
Rothwell
,
B.
, and
Robinson
,
T.
, “
Measurements of Decompression Wave Speed in Anthropogenic Carbon Dioxide Mixtures Containing Hydrogen
,”
ASME J. Pressure Vessel Technol.
(submitted).
24.
Botros
,
K. K.
,
Geerligs
,
J.
,
Rothwell
,
B.
, and
Robinson
,
T.
, “
Measurements of Decompression Wave Speed in Anthropogenic Carbon Dioxide Mixtures Containing Argon
,”
ASME J. Pressure Vessel Technol. (submitted).
25.
Kunz
,
R.
,
Klimeck
,
W.
,
Wagner
,
M.
, and
Jaeschke
,
M.
,
2007
, “
The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures
,” Groupe Européen de Recherches Gaziéres (
GERG
), Brussels, Belgium, Technical Monograph No. GERG TM15.
26.
Peng
,
D. Y.
, and
Robinson
,
D. B.
,
1976
, “
A New Two-Constant Equation of State
,”
Ind. Eng. Chem. Fundam.
,
15
(
1
), pp.
59
64
.
27.
Lemmon
,
E. W.
,
Huber
,
M. L.
, and
McLinden
,
M. O.
,
2010
, “
NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties—REFPROP, Version 9.0
,” National Institute of Standards and Technology, Standard Reference Data Program, Gaithersburg, MD.
28.
Cosham
,
A.
,
Jones
,
D. G.
,
Armstrong
,
K.
,
Allason
,
D.
, and
Barnett
,
J.
,
2014
, “
Analysis of Two Dense Phase Carbon Dioxide Full-Scale Fracture Propagation Test
,”
ASME
Paper No. IPC2014-33080.
29.
Eiber
,
R.
,
Bubenik
,
T.
, and
Maxey
,
W. A.
, 1993, “
GASDECOM, Computer Code for the Calculation of Gas Decompression Speed
,”
Fracture Control Technology for Natural Gas Pipelines
, by R. Eiber, T. Bubenik, and W.A. Maxey, American Gas Association, Washington, DC, NG-18 Report 208, A.G.A. Catalogue No. L51691.
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