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Adsorption equilibrium and kinetics of CO2, CH4 and N2 on zeolite BETA with different cations and SiO2/Al2O3 ratio

dc.contributor.authorHenrique, Adriano
dc.contributor.authorSilva, José A.C.
dc.contributor.authorRodrigues, Alírio
dc.date.accessioned2020-03-02T16:14:28Z
dc.date.available2020-03-02T16:14:28Z
dc.date.issued2017
dc.description.abstractBiogas is a gas mixture obtained by the anaerobic decomposition of organic matter, being mainly composed by methane, carbon dioxide and other compounds in minor amounts, such as nitrogen, hydrogen sulfide, water vapor and others. Due to the high quantity of methane (higher than 50%), the biogas can be used as a fuel, but, it’s necessary to go through a process of purification, to remove CO2 and transform it in biomethane (around 95%), a fuel similar to natural gas [1,2]. In this way, gas adsorption equilibrium of CO2, CH4 and N2 were investigated in three different types of zeolite BETA materials namely H-BETA-25, Na-BETA-25 and H-BETA-150 at temperatures 313, 373 and 423 K under partial pressures between 0.33 and 4.16 bar. For this experimental analysis a gas chromatographic system was utilized. The isotherm data has been satisfactorily demonstrated with the Langmuir model and the amount adsorbed follows the decreasing order as CO2 > CH4 > N2 for all materials used. Considering experimental temperature, all materials show better absorption at the lowest temperature (313 K) for obvious reason. First, when we compare two zeolites containing the same SiO2/Al2O3 molar ratio but different compensation cations (H-BEA-25 and Na-BEA-25), interesting results are obtained. It is found that only due to presence of Na+ cationic center, zeolite Na-BETA-25 adsorbed quite higher amount of gases than H-BETA-25 (2.84, 1.59 and 0.97 mol/kg, and 2.28, 1.31 and 0.83 mol/kg respectively of CO2, CH4 and N2 gases at 313 K). In second comparison between two different SiO2/Al2O3 molar ratio (H-BETA-25 and H-BETA-150), zeolite H-BETA-25 adsorbed a little bit higher amount of gases than H-BETA-150 (2.23, 0.98 and 0.58 mol/kg). But when we consider selectivity of gases the zeolite H-BETA-150 (adsorbs lowest amount of gases) showed to be the best over other two materials with decreasing value in pair order CO2/N2 > CO2/CH4 > CH4/N2 (6.65, 3.24 and 2.05 at 313 K). The selectivity order is the same for all three zeolites at mentioned temperatures. The mass transfer studies were made using the Zero Length Column (ZLC) technique, at 313 K. But it is very difficult to determine the mechanism that controls the diffusion onto three zeolites, as experiments are so fast that ZLC studies were made in equilibrium conditions. Accordingly, it was not possible to obtain kinetic information for the adsorbents. However, it can be said that there are no resistances to the mass transfer in the studied conditions.pt_PT
dc.description.versioninfo:eu-repo/semantics/publishedVersionpt_PT
dc.identifier.citationHenrique, Adriano; Silva, José A.C.; Rodrigues, Alírio E. (2017). Adsorption equilibrium and kinetics of CO2, CH4 and N2 on zeolite BETA with different cations and SiO2/Al2O3 ratio. In 10º Encontro Nacional de Cromatografia. Instituto Politécnico de Bragança. ISBN 978-972-745-234-7pt_PT
dc.identifier.isbn978-972-745-234-7
dc.identifier.urihttp://hdl.handle.net/10198/20792
dc.language.isoengpt_PT
dc.peerreviewedyespt_PT
dc.publisherInstituto Politécnico de Bragançapt_PT
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/pt_PT
dc.subjectAdsorptionpt_PT
dc.titleAdsorption equilibrium and kinetics of CO2, CH4 and N2 on zeolite BETA with different cations and SiO2/Al2O3 ratiopt_PT
dc.typeconference object
dspace.entity.typePublication
oaire.citation.conferencePlaceInstituto Politécnico de Bragançapt_PT
oaire.citation.startPage27pt_PT
oaire.citation.title10º Encontro Nacional de Cromatografiapt_PT
person.familyNameHenrique
person.familyNameSilva
person.givenNameAdriano
person.givenNameJosé A.C.
person.identifier.ciencia-idDB18-4E7D-6696
person.identifier.ciencia-idC11B-F5CF-7C78
person.identifier.orcid0000-0002-5227-9790
person.identifier.orcid0000-0003-1778-3833
person.identifier.scopus-author-id7403023684
rcaap.rightsopenAccesspt_PT
rcaap.typeconferenceObjectpt_PT
relation.isAuthorOfPublication8f18b8ea-087b-4626-b5f1-9b66b1aa993f
relation.isAuthorOfPublication16366ede-a7d6-45ff-a8c9-eff9bdde35c7
relation.isAuthorOfPublication.latestForDiscovery16366ede-a7d6-45ff-a8c9-eff9bdde35c7

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