Simulation-based techno-economic evaluation for optimal design of CO 2 transport pipeline network

For large volumes of carbon dioxide (CO2) 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 CO2 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 CO2 compression train and the trunk pipelines respectively. The evaluation results were compared with other published cost models. Optimal options of compression train and trunk pipelines were applied to form an optimal case. The overall cost of CO2 transport pipeline network was analyzed and compared between the base case and the optimal case. The results show the optimal case has an annual saving of 22.7M€. For the optimal case, levelized energy and utilities cost is 7.62€/t-CO2, levelized capital cost of trunk pipeline is about 8.11€/t-CO2 and levelized capital cost of collecting system is 2.62€/t- CO2. The overall levelized cost of the optimal case was also compared to the result of another project to gain more insights for CO2 pipeline network design.

[1]  Hailong Li,et al.  Impurity impacts on the purification process in oxy-fuel combustion based CO2 capture and storage system , 2009 .

[2]  Julia Race,et al.  Towards a CO2 pipeline specification : defining tolerance limits for impurities , 2012 .

[3]  Jinyue Yan,et al.  Impacts of equations of state (EOS) and impurities on the volume calculation of CO2 mixtures in the applications of CO2 capture and storage (CCS) processes , 2009 .

[4]  P Freund Making deep reductions in CO 2 emissions from coal-fired power plant using capture and storage of CO 2 , 2003 .

[5]  Andrzej Witkowski,et al.  Comprehensive analysis of pipeline transportation systems for CO2 sequestration. Thermodynamics and safety problems , 2013 .

[6]  Simon Roussanaly,et al.  Costs benchmark of CO2 transport technologies for a group of various size industries , 2013 .

[7]  Hubertus Tummescheit,et al.  Dynamic simulation of a carbon dioxide transfer pipeline for analysis of normal operation and failure modes , 2011 .

[8]  Joan M. Ogden,et al.  Techno-Economic Models for Carbon Dioxide Compression, Transport, and Storage & Correlations for Estimating Carbon Dioxide Density and Viscosity , 2006 .

[9]  Rickard Svensson,et al.  Transportation systems for CO2––application to carbon capture and storage , 2004 .

[10]  Ning Wei,et al.  Regional Opportunities for Carbon Dioxide Capture and Storage in China: A Comprehensive CO2 Storage Cost Curve and Analysis of the Potential for Large Scale Carbon Dioxide Capture and Storage in the People’s Republic of China , 2009 .

[11]  Byung-Ik Lee,et al.  A generalized thermodynamic correlation based on three‐parameter corresponding states , 1975 .

[12]  Michael Klett,et al.  The Economics of CO 2 Storage , 2003 .

[13]  Bert Metz,et al.  Carbon Dioxide Capture and Storage , 2005 .

[14]  Jinyue Yan,et al.  Impact of Impurities in CO2-Fluids on CO2 Transport Process , 2006 .

[15]  Young-il Kim,et al.  Equation of state for carbon dioxide , 2007 .

[16]  W. Wagner,et al.  The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004 , 2012 .

[17]  Andrzej J. Osiadacz,et al.  Dynamic simulation of pipelines containing dense phase/supercritical CO2-rich mixtures for carbon capture and storage , 2012 .

[18]  D. Peng,et al.  A New Two-Constant Equation of State , 1976 .

[19]  Michael Klett,et al.  The Economics of CO2 Storage , 2003 .

[20]  Fariba Dehghani,et al.  MODELING OF PHASE EQUILIBRIA FOR BINARY AND TERNARY MIXTURES OF CARBON DIOXIDE , HYDROGEN AND METHANOL , 2003 .

[21]  Hailong Li,et al.  PVTxy properties of CO2 mixtures relevant for CO2 capture, transport and storage: Review of available experimental data and theoretical models , 2011 .

[22]  Ioannis G. Economou,et al.  Evaluation of Cubic, SAFT, and PC-SAFT Equations of State for the Vapor–Liquid Equilibrium Modeling of CO2 Mixtures with Other Gases , 2013 .

[23]  W. Wagner,et al.  A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple‐Point Temperature to 1100 K at Pressures up to 800 MPa , 1996 .

[24]  André Faaij,et al.  A state-of-the-art review of techno-economic models predicting the costs of CO2 pipeline transport , 2013 .

[25]  M. Wertheim,et al.  Fluids with highly directional attractive forces. II. Thermodynamic perturbation theory and integral equations , 1984 .

[26]  Bjørn Kvamme,et al.  Consequences of CO2 solubility for hydrate formation from carbon dioxide containing water and other impurities. , 2014, Physical chemistry chemical physics : PCCP.

[27]  Aie,et al.  Energy Technology Perspectives 2012 , 2006 .

[28]  Claire S. Adjiman,et al.  Modeling the Fluid Phase Behavior of Carbon Dioxide in Aqueous Solutions of Monoethanolamine Using Transferable Parameters with the SAFT-VR Approach , 2010 .

[29]  Charles Eickhoff,et al.  Effect of Common Impurities on the Phase Behavior of Carbon-Dioxide-Rich Systems: Minimizing the Risk of Hydrate Formation and Two-Phase Flow , 2011 .

[30]  Edward S. Rubin,et al.  An engineering-economic model of pipeline transport of CO2 with application to carbon capture and storage , 2008 .

[31]  K. Jordal,et al.  Gas conditioning—The interface between CO2 capture and transport , 2007 .

[32]  M. Wertheim,et al.  Fluids with highly directional attractive forces. I. Statistical thermodynamics , 1984 .

[33]  H Mahgerefteh,et al.  PRESSURISED CO2 PIPELINE RUPTURE , 2008 .

[34]  Eric Williams,et al.  Potential economies of scale in CO2 transport through use of a trunk pipeline , 2010 .

[35]  Meihong Wang,et al.  Post-combustion CO2 capture with chemical absorption: A state-of-the-art review , 2011 .

[36]  Julia Race,et al.  Transporting the Next Generation of CO2 for Carbon, Capture and Storage: The Impact of Impurities on Supercritical CO2 Pipelines , 2008 .

[37]  Zaoxiao Zhang,et al.  Optimization of pipeline transport for CO2 sequestration , 2006 .

[38]  W. Nijs,et al.  Policy Support System for Carbon Capture and Storage «PSS-CCS» , 2009 .

[39]  Jens Hetland,et al.  Cost Analysis of CO2 Transportation: Case Study in China , 2011 .

[40]  Hans Joachim Krautz,et al.  Modelling of the CO2 process- and transport chain in CCS systems—Examination of transport and storage processes , 2010 .

[41]  Joan M. Ogden CONCEPTUAL DESIGN OF OPTIMIZED FOSSIL ENERGY SYSTEMS WITH CAPTURE AND SEQUESTRATION OF CARBON DIOXIDE , 2004 .

[42]  Frances E. Pereira,et al.  Transferable SAFT-VR models for the calculation of the fluid phase equilibria in reactive mixtures of carbon dioxide, water, and n-alkylamines in the context of carbon capture. , 2011, The journal of physical chemistry. B.

[43]  Ton Wildenborg,et al.  Designing a cost-effective CO2 storage infrastructure using a GIS based linear optimization energy model , 2010, Environ. Model. Softw..

[44]  G. Soave Equilibrium constants from a modified Redlich-Kwong equation of state , 1972 .

[45]  Meihong Wang,et al.  Case study on CO2 transport pipeline network design for Humber region in the UK , 2014 .

[46]  P. Freund,et al.  Making deep reductions in CO2 emissions from coal-fired power plant using capture and storage of CO2 , 2003 .

[47]  Andrea Ramírez,et al.  The impact of CO2 capture in the power and heat sector on the emission of SO2, NOx, particulate matter, volatile organic compounds and NH3 in the European Union , 2010 .

[48]  Hailong Li,et al.  Evaluating cubic equations of state for calculation of vapor–liquid equilibrium of CO2 and CO2-mixtures for CO2 capture and storage processes , 2009 .

[49]  M. Wertheim,et al.  Fluids with highly directional attractive forces. IV. Equilibrium polymerization , 1986 .