As part of efforts to mitigate the global effects of greenhouse gases from fossil fuels, CO2 Capture and Storage (ccs) technology has drawn large attention from the engineering research community. Compared to a pipeli...
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As part of efforts to mitigate the global effects of greenhouse gases from fossil fuels, CO2 Capture and Storage (ccs) technology has drawn large attention from the engineering research community. Compared to a pipeline-based system, an offshore ccssystem using Liquefied CO2 (LCO2) carrier ships and offshore oil wells is expected to offer a more flexible and efficient mode of ccs to many countries, especially nations such as Korea where a pipeline-based system is inherently infeasible. In this paper we discuss a carrier-based offshore ccssystem, in which CO2 carriers may transport crude oils on inbound voyage, and seek the optimal configuration of the system including liquefaction plant location, fleet assignment, and the optimal pressure and temperature of the cargo CO2. We determine the optimal system configuration including the liquefaction plant location and CO2 carrier fleet assignment with respect to the overall transport cost of the ccssystem. We use two sequential linear programming problems - plant location and fleet assignment, with the pressure and temperature state of cargo CO2 as the key ccs chain parameters. We find that the optimal state of CO2 at each stage in the system can deviate from the triple point, depending on the system's configuration and throughput. As a case study, we demonstrate that the optimal cargo state can be different from the triple point depending on the system configuration. In this case it is -39 degrees C and 10 bar and the overall transport cost of CO2 sequestration is 26.7 USD/ton. This result is based on the specific scenario of the CO2 Capture and Storage system for Korea using southeastern Asian offshore oil wells. (C) 2012 Elsevier Ltd. All rights reserved.
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