2008
DOI: 10.1016/s1750-5836(07)00119-3
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An engineering-economic model of pipeline transport of CO2 with application to carbon capture and storage

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Cited by 313 publications
(223 citation statements)
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“…If the cost of storage varies on the same scale as the cost of transport reported in literature, which our analysis supports, the optimal transport configuration must take into account variations in storage capacity (Gresham et al, 2010;McCoy and Rubin, 2008;Middleton and Bielicki, 2009). Without differentiating the cost at the end of the transport stage, the transport optimization algorithm will not map cost-efficient or possibly even practical routes for transporting CO 2 from sources to sinks.…”
Section: Discussionmentioning
confidence: 67%
See 1 more Smart Citation
“…If the cost of storage varies on the same scale as the cost of transport reported in literature, which our analysis supports, the optimal transport configuration must take into account variations in storage capacity (Gresham et al, 2010;McCoy and Rubin, 2008;Middleton and Bielicki, 2009). Without differentiating the cost at the end of the transport stage, the transport optimization algorithm will not map cost-efficient or possibly even practical routes for transporting CO 2 from sources to sinks.…”
Section: Discussionmentioning
confidence: 67%
“…To date, studies using transport modeling have done the best job integrating the cost of transportation and storage. Middleton andBielicki(2009), McCoy andRubin (2008), and Wildenborg et al (2004) among others have developed transport optimization algorithms that can take into account geologic and economic differences between storage sites. The disclosure of costs in these studies, however, is generally in the form of summary statistics (e.g.…”
Section: Discussionmentioning
confidence: 99%
“…In large-scale pipeline transport, CO2 is mostly in a liquid or supercritical phase [15,16]. Therefore, it should be compressed to a pressure higher than the critical pressure of 7.38 MPa to change the phase to a liquid or supercritical state.…”
Section: Design Of Pipeline Transportmentioning
confidence: 99%
“…Therefore, it should be compressed to a pressure higher than the critical pressure of 7.38 MPa to change the phase to a liquid or supercritical state. In this study, the minimum pressure in the pipeline was set not to the critical pressure but to 8.6 MPa to avoid abrupt changes in the compressibility of CO2 [10,15]. The maximum pressure was set to 15 MPa to avoid exceeding the maximum allowable operating pressure of ASME-ANSI 900# flanges [15].…”
Section: Design Of Pipeline Transportmentioning
confidence: 99%
“…From the power plant, the CO 2 is then transported to the EOR project via pipeline. For pipeline transport over short distances (less than 100 km), we assume that no additional energy from what is used at the power plant to compress the CO 2 (and which is included in the efficiency of the power plant) is required for pumping (23). For longer pipeline transport (1000 km), 6.5 kWh of electricity are needed per metric ton of CO 2 transported for pumping (1).…”
Section: Life Cycle Emissions Of Fuels Used Within the Systemmentioning
confidence: 99%