Design, process simulation and construction of a 100 kW pilot-scale CO2 membrane rig: Improving in situ CO2 capture using selective exhaust gas recirculation (S-EGR)

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dc.contributor.authorDarabkhani, Hamidreza Gohari
dc.contributor.authorJurado Pontes, Nelia
dc.contributor.authorPrpich, George
dc.contributor.authorOakey, John E.
dc.contributor.authorWagland, Stuart T.
dc.contributor.authorAnthony, Edward J.
dc.date.accessioned2017-12-19T11:27:06Z
dc.date.available2017-12-19T11:27:06Z
dc.date.issued2017-12-01
dc.description.abstractCarbon capture and storage (CCS) from natural gas-fired systems is an emerging field and many of the concepts and underlying scientific principles are still being developed. Preliminary studies suggest this approach can boost the CO2 content in the feed gas up to 3 times compared to the ‘no recycle’ case (CO2 concentration increased to 18% vs. 6%), with a consequent reduction in flow to the post-combustion capture unit by a factor of three compared to conventional, non-S-EGR. For this project, Cranfield University developed a pilot-scale 100 kW CO2 membrane rig facility in order to investigate simultaneously EGR and S-EGR technologies, the latter being achieved by using a CO2 sweep air polymeric membrane. A bench-scale membrane rig has also been developed to investigate the permeability and selectivity of different polymeric membranes to CO2. Currently a small-scale polydimethylsiloxane (PDMS) membrane module is also being investigated to study its selectivity/permeability. The tests include exploring the performance improvement of the PDMS membrane using different operating conditions with a view to developing scale-up procedures for the membrane unit for the actual 100 kW pilot-scale rig. Process simulations were performed using Aspen Plus software to predict the behaviour of the pilot-scale rig using a model developed based on empirical parameters (i.e., mass transfer coefficient of CO2 through the membrane and permeance), measured in the bench-scale membrane test unit. The results show that CO2 concentrations of up to 14.9% (comparable to CO2 level in coal combustion) can be achieved with 60% EGR, with a 90% CO2 removal efficiency of the membrane units. However, the results generated with the membrane model in which specific permeance values to PDMS were applied, predicted concentrations of CO2 in flue gases up to 9.8% (v/v) for a selective recycle of 60%. The study shows that the S-EGR technique is an effective method that can provide similar conditions to that of a coal-fired power plant for the post-combustion capture system operating on natural gas-fired units, but also highlights the fact that more research is required to find more suitable materials for membranes that optimise the CO2 removal efficiencies from the flue gas.en_UK
dc.identifier.citationHamidreza G. Darabkhani, Nelia Jurado, et al., (2018) Design, process simulation and construction of a 100 kW pilot-scale CO2 membrane rig: Improving in situ CO2 capture using selective exhaust gas recirculation (S-EGR). Journal of Natural Gas Science and Engineering, Volume 50, February 2018, pp. 128-138en_UK
dc.identifier.issn1875-5100
dc.identifier.urihttps://doi.org/10.1016/j.jngse.2017.09.012
dc.identifier.urihttp://dspace.lib.cranfield.ac.uk/handle/1826/12791
dc.language.isoenen_UK
dc.publisherElsevieren_UK
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 International*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subjectCarbon dioxide captureen_UK
dc.subjectGas-CCSen_UK
dc.subjectExhaust gas recirculation (EGR)en_UK
dc.subjectCO2 selective membraneen_UK
dc.subjectSelective EGR (S-EGR)en_UK
dc.titleDesign, process simulation and construction of a 100 kW pilot-scale CO2 membrane rig: Improving in situ CO2 capture using selective exhaust gas recirculation (S-EGR)en_UK
dc.typeArticleen_UK

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