2014
DOI: 10.1016/j.apenergy.2014.07.063
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Simulation-based techno-economic evaluation for optimal design of CO 2 transport pipeline network

Abstract: For large volumes of carbon dioxide (CO 2 ) onshore and offshore transportation, pipeline is considered the preferred method. This paper presents a study of the pipeline network planned in the Humber region of the UK. Steady state process simulation models of the CO 2 transport pipeline network were developed using Aspen HYSYS ® . The simulation models were integrated with Aspen Process Economic Analyser ® (APEA). In this study, techno-economic evaluations for different options were conducted for the CO 2 comp… Show more

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Cited by 67 publications
(29 citation statements)
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“…To date, no EOS is specifically recommended for CO 2 mixtures, but the ability to accurately predict the Vapour Liquid Equilibrium (VLE), density and speed of sound is considered the best way to gauge any weaknesses or strengths of EOS [2,8,38,39]. Li et al [2,8] has not been implemented in CFD models of decompression or outflow models to date , though it is currently the reference EOS for natural gas [50].…”
Section: Computational Fluid Dynamics (Cfd) Technique Have Been Develmentioning
confidence: 99%
“…To date, no EOS is specifically recommended for CO 2 mixtures, but the ability to accurately predict the Vapour Liquid Equilibrium (VLE), density and speed of sound is considered the best way to gauge any weaknesses or strengths of EOS [2,8,38,39]. Li et al [2,8] has not been implemented in CFD models of decompression or outflow models to date , though it is currently the reference EOS for natural gas [50].…”
Section: Computational Fluid Dynamics (Cfd) Technique Have Been Develmentioning
confidence: 99%
“…The CO 2 compression train is not only an expensive equipment but also a big power consumer [14]. Witkowski et al [15] dissected the power requirements of different configurations of CO 2 compression train are from 57.8 to 31.3 MW e for a capture-ready 900 MW e hard coal-fired power plant.…”
Section: Previous Studiesmentioning
confidence: 99%
“…A basic post combustion installation based on MEA absorption process was assumed and with the use of process simulator, taking the overall efficiency of The operating pressure range of the pipeline infrastructure was set to (8)(9)(10)(11)(12)(13)(14)(15) MPa in order to maintain the post combustion CO2-rich mixture in supercritical phase. As a result the pipeline wall thickness for the whole network was chosen equal to 25 mm.…”
Section: Basic Assumptions and Input Datamentioning
confidence: 99%
“…Least cost optimisation model of an integrated CO2 capture, transportation and storage infrastructure for the UK over four time periods up to year 2050 was presented in the study by Elahi et al [9]. The physical characteristics of a potential pipeline network for CO2 transportation in the Humber Region in the UK area have been discussed by Luo et al [10]. Hetland et al [11] present the status of the large European CCS demonstration projects with particular emphasis on transport systems development.…”
Section: Introductionmentioning
confidence: 99%