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Design, techno-economic evaluation, and optimisation of renewable methanol plant model: Finland case study

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dc.title Design, techno-economic evaluation, and optimisation of renewable methanol plant model: Finland case study en
dc.contributor.author Emebu, Samuel
dc.contributor.author Mendoza Martinez, Clara
dc.contributor.author Omoregbe, Osaze
dc.contributor.author Mankonen, Aleksi
dc.contributor.author Ogbuoji, Ebuka A.
dc.contributor.author Shaikh, Ibrahim
dc.contributor.author Pettersen, Even
dc.contributor.author Kubalčík, Marek
dc.contributor.author Okieimen, Charity
dc.relation.ispartof Chemical Engineering Science
dc.identifier.issn 0009-2509 Scopus Sources, Sherpa/RoMEO, JCR
dc.identifier.issn 1873-4405 Scopus Sources, Sherpa/RoMEO, JCR
dc.date.issued 2023
utb.relation.volume 278
dc.type article
dc.language.iso en
dc.publisher Elsevier Ltd
dc.identifier.doi 10.1016/j.ces.2023.118888
dc.relation.uri https://www.sciencedirect.com/science/article/pii/S000925092300444X
dc.relation.uri https://www.sciencedirect.com/science/article/pii/S000925092300444X/pdfft?md5=36c1c72cb0e7b0b83d99accd776a836f&pid=1-s2.0-S000925092300444X-main.pdf
dc.subject central composite design (CCD) en
dc.subject optimisation en
dc.subject manufacturing unit cost en
dc.subject conversion of carbon dioxide en
dc.subject Langmuir-Hinshelwood-Hougen-Watson (LHHW) en
dc.subject cost-to-size model en
dc.description.abstract The current global energy crisis, emphasises the need to simultaneously reduce fossil energy consumption, accelerate renewable energy development, and mitigate global warming, which may arise from situations of dirtier fuel usage. Consequently, this work highlights how captured carbon dioxide from fossil power and manufacturing plants, together with hydrogen purportedly produced via water electrolysis (powered by residual energy from fossil and renewable power plants), can be used to synthesize methanol. Therefore, a methanol plant model was proposed and designed. Multivariable regressions for the plant model were developed and optimised. Furthermore, deduced optimal were used to develop a Langmuir-Hinshelwood-Hougen-Watson (LHHW) kinetic equivalent to the Gibbs reaction model used in the simulation. Also, the plant cost analysis was performed at the optimal, and hydrogen cost was found to constitute the highest manufacturing cost component, hence the costdetermining factor of the plant. Finally, cost-to-size models for various cost components were also deduced. en
utb.faculty Faculty of Applied Informatics
dc.identifier.uri http://hdl.handle.net/10563/1011554
utb.identifier.obdid 43884581
utb.identifier.scopus 2-s2.0-85160101454
utb.identifier.wok 001005419400001
utb.identifier.coden CESCA
utb.source j-scopus
dc.date.accessioned 2023-07-19T10:39:37Z
dc.date.available 2023-07-19T10:39:37Z
dc.description.sponsorship IGA/CebiaTech/2023/004; U.S. Department of Energy, USDOE; Anhui University of Technology, AHUT; Univerzita Tomáše Bati ve Zlíně
dc.description.sponsorship Department of Energy; Internal Grant Agency [IGA/CebiaTech/2023/004]; Tomas Bata University
dc.rights Attribution 4.0 International
dc.rights.uri http://creativecommons.org/licenses/by/4.0/
dc.rights.access openAccess
utb.ou Department of Automatic Control and Informatics
utb.contributor.internalauthor Emebu, Samuel
utb.contributor.internalauthor Shaikh, Ibrahim
utb.fulltext.sponsorship This work was supported by the Department of Energy, Lappeenranta - Lahti University of Technology, and the Internal Grant Agency (IGA/CebiaTech/2023/004) of Tomas Bata University.
utb.wos.affiliation [Emebu, Samuel; Shaikh, Ibrahim; Kubalc, Marek] Tomas Bata Univ Zlin, Fac Appl Informat, Dept Automatic Control & Informat, Nad Stranemi 4511, Zlin 76005, Czech Republic; [Martinez, Clara Mendoza; Mankonen, Aleksi] Lappeenranta Lahti Univ Technol LUT, DOE, Yliopistonkatu 34, Lappeenranta 53850, Finland; [Omoregbe, Osaze] Univ Birmingham, Ctr Fuel Cell & Hydrogen Res, Sch Chem Engn, Birmingham B152TT, England; [Pettersen, Even] Norwegian Univ Sci & Technol, Dept Chem Engn, Hogskoleringen 1, N-7491 Trondheim, Norway; [Emebu, Samuel; Omoregbe, Osaze; Okieimen, Charity] Univ Benin, Fac Engn, Dept Chem Engn, POB 1154, Benin, Nigeria; [Ogbuoji, Ebuka A.] Univ Kentucky, Dept Chem & Mat Engn, Lexington, KY 40506 USA
utb.scopus.affiliation Department of Automatic Control and Informatics, Faculty of Applied Informatics, Tomas Bata University in Zlín, Nad Stráněmi 4511, Zlín, 760 05, Czech Republic; Department of Energy, Lappeenranta-Lahti University of Technology LUT, Yliopistonkatu 34, Lappeenranta, FI-53850, Finland; Centre for Fuel Cell and Hydrogen Research, School of Chemical Engineering, University of Birmingham, Edgbaston, Birmingham, B15 2TT, United Kingdom; Department of Chemical Engineering, Norwegian University of Science and Technology, Høgskoleringen 1, Trondheim, 7491, Norway; Department of Chemical Engineering, Faculty of Engineering, University of Benin, PO Box 1154, Benin City, Nigeria; Department of Chemical and Materials Engineering, University of Kentucky, Lexington, KY 40506, United States
utb.fulltext.projects IGA/CebiaTech/2023/004
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Attribution 4.0 International Kromě případů, kde je uvedeno jinak, licence tohoto záznamu je Attribution 4.0 International