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CFD Simulation of CO2 and Methane Adsorption at Various Temperature for MOF-5 using Dual-site and Single-site Langmuir Model

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dc.citedby5
dc.contributor.authorZulkifli M.Z.A.en_US
dc.contributor.authorMukhtar A.en_US
dc.contributor.authorFadli M.F.M.en_US
dc.contributor.authorBahari A.M.S.en_US
dc.contributor.authorMatsumoto A.en_US
dc.contributor.authorMisran H.en_US
dc.contributor.authorid57408748100en_US
dc.contributor.authorid57195426549en_US
dc.contributor.authorid57411757600en_US
dc.contributor.authorid57411619300en_US
dc.contributor.authorid14525231700en_US
dc.contributor.authorid6506899840en_US
dc.date.accessioned2023-05-29T09:05:44Z
dc.date.available2023-05-29T09:05:44Z
dc.date.issued2021
dc.description.abstractThe annual increase in energy demand has led to an increase in greenhouse gas emissions, in particular CO2 emissions from the power generation industry. Carbon Capture and Utilization are technologies applied to capture CO2 gases and transform the gases into a different energy source. The adsorption technology to capture CO2 gases was chosen due to the minimum energy consumption and low costs required for an industrial application for sustainability. Metal-Organic Framework (MOF) has a reasonably high CO2 adsorption capability. It has been applied as an adsorbent for capturing and storing CO2. In this study, a comparison of CFD simulation with experimental CO2 and methane adsorption values in solid adsorbent beds containing MOF-5 at various temperatures was presented. The simulation was performed using 2D and 3D models from 0? at STP to 130? for CO2 and methane gas molecules. In addition, the isothermal and kinetic adsorption model was added to the simulations. This includes Single-and Dual-Site Langmuir adsorption isotherm and Linear Driving Force. The porous media model was then activated to imitate packed bed adsorbent and measured the pressure drop from the simulation. The results showed that the CO2 adsorption values of MOF-5 decrease as the adsorbent temperature increases. There was a decline of 0.002 mmol/g of adsorbed CO2 molecules per 10-kelvin difference. The CO2 adsorption value was 0.53 mmol/g at STP and 1.15 mmol/g for CH4 at STP. Both CO2 and CH4 adsorption were used to suggest optimal CO2 adsorption for the Pressure Swing Adsorption cycle. � 2021, Penerbit Akademia Baru. All rights reserved.en_US
dc.description.natureFinalen_US
dc.identifier.doi10.37934/cfdl.13.10.110
dc.identifier.issue10
dc.identifier.scopus2-s2.0-85122815036
dc.identifier.urihttps://www.scopus.com/inward/record.uri?eid=2-s2.0-85122815036&doi=10.37934%2fcfdl.13.10.110&partnerID=40&md5=ab1617de6b5631b6bd33f65cb53690a5
dc.identifier.urihttps://irepository.uniten.edu.my/handle/123456789/25953
dc.identifier.volume13
dc.publisherPenerbit Akademia Baruen_US
dc.relation.ispartofAll Open Access, Hybrid Gold
dc.sourceScopus
dc.sourcetitleCFD Letters
dc.titleCFD Simulation of CO2 and Methane Adsorption at Various Temperature for MOF-5 using Dual-site and Single-site Langmuir Modelen_US
dc.typeArticleen_US
dspace.entity.typePublication
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