2014
DOI: 10.1016/b978-0-444-63455-9.50107-0
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Process Simulation and Analysis for CO2 Transport Pipeline Design and Operation – Case Study for the Humber Region in the UK

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Cited by 8 publications
(4 citation statements)
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“…The third significant contribution to the overall CCS energy cost is represented by CO 2 compression. The specific energy consumption is equal to 80 kWh e /t CO2 (13 MW e ) and 98 kWh e /t CO2 (16 MW e ) for MEA and HPC, respectively, which is in line with values reported in the literature [78]. The former is lower thanks to the higher regeneration pressure in the stripper.…”
Section: Process Simulationssupporting
confidence: 88%
“…The third significant contribution to the overall CCS energy cost is represented by CO 2 compression. The specific energy consumption is equal to 80 kWh e /t CO2 (13 MW e ) and 98 kWh e /t CO2 (16 MW e ) for MEA and HPC, respectively, which is in line with values reported in the literature [78]. The former is lower thanks to the higher regeneration pressure in the stripper.…”
Section: Process Simulationssupporting
confidence: 88%
“…Consequently, current operating practice for CO 2 pipelines is to maintain the pressure well above the critical pressure. Considering the pressure drop along the length of the pipeline and the impact of the elevation change and impurities, the entry pressure of the CO 2 pipeline network could be as high as 110-150 bar [9,14,52,53]. Thus a compression train is required to pressurize the CO 2 stream from PCC captured plant to reach such a high entry pressure.…”
Section: Co 2 Compression Technologymentioning
confidence: 98%
“…After the CO 2 captured from the power plant, it will be pressurized at a pressure as high as 110-150 bar for pipeline transport and geologic sequestration [32,33]. Thus a compression train is needed.…”
Section: Simulation Of Compression Processmentioning
confidence: 99%