Synthetic natural gas production through biogas methanation using a sorption-enhanced reaction process

dc.contributor.authorCañada Barcala, Andrés
dc.contributor.authorLarriba Martínez, Marcos
dc.contributor.authorÁgueda Maté, Vicente Ismael
dc.contributor.authorDelgado Dobladez, José Antonio
dc.date.accessioned2024-06-20T09:08:34Z
dc.date.available2024-06-20T09:08:34Z
dc.date.issued2024-03
dc.description.abstractUsing CO2 from biogenic sources to produce fuels is one of the most attractive applications in climate change mitigation, as it leads to the replacement of fossil fuels and contributes to the circular economy. By this means, the primary purpose of this paper is to design a biogas methanation process to produce synthetic natural gas (SNG) suitable to be fed into the gas grid. In this way, a SERP process was proposed in which the equilibrium is overcome by eliminating the co-produced water using a selective adsorbent, such as zeolite 3A. For this purpose, two different catalysts were (NiAl2O3 and Ni5A) and compared with a commercial catalyst. First, the catalytic performance of the three catalysts was studied in an experimental setup, discarding the Ni5A catalyst due to its lower reaction yields. Subsequently, a sorption-enhanced reaction process (SERP) was designed by simulation using the experimental kinetic data obtained and a theoretical model of reaction/adsorption cycles design. The PSASIM software, previously registered by the research group, was used for the simulation. The proposed process consisted of three main stages: a first reaction/adsorption stage where the biogas was upgraded to SNG with the corresponding water adsorption by the catalyst/adsorbent, and a second and third stages (purge and rinse) where the retained water in the adsorbent is desorbed and eliminated from the process. The process variables studied were temperature and biogas composition fed to the process. Finally, at 488 K and a residual waste biogas composition (55–60 % CH4), CO2 conversions of 99.55 % and selectivities towards methane of 99.99 % were achieved using NiAl2O3-zeolite3A mixture. In addition, the purity of the methane produced was 98.6 % molar in the product.
dc.description.departmentDepto. de Ingeniería Química y de Materiales
dc.description.facultyFac. de Ciencias Químicas
dc.description.fundingtypeDescuento UCM
dc.description.refereedTRUE
dc.description.statuspub
dc.identifier.citationAndrés Cañada-Barcala, Marcos Larriba, Vicente Ismael Águeda Maté, José Antonio Delgado Dobladez, Synthetic natural gas production through biogas methanation using a sorption-enhanced reaction process, Separation and Purification Technology, Volume 331, 2024, 125714, ISSN 1383-5866,
dc.identifier.doi10.1016/j.seppur.2023.125714
dc.identifier.issn1383-5866
dc.identifier.officialurlhttps://doi. org/10.1016/j.seppur.2023.125714.
dc.identifier.relatedurlhttps://www.sciencedirect.com/journal/separation-and-purification-technology
dc.identifier.urihttps://hdl.handle.net/20.500.14352/105111
dc.journal.titleSeparation and Purification Technology
dc.language.isoeng
dc.page.initial125714
dc.publisherElsevier
dc.rightsAttribution-NoDerivatives 4.0 Internationalen
dc.rights.accessRightsopen access
dc.rights.urihttp://creativecommons.org/licenses/by-nd/4.0/
dc.subject.cdu66.0
dc.subject.keywordBiogas upgrading
dc.subject.keywordSERP process
dc.subject.keywordMethanation
dc.subject.keywordCO2 utilization
dc.subject.ucmIngeniería química
dc.subject.unesco3303 Ingeniería y Tecnología Químicas
dc.titleSynthetic natural gas production through biogas methanation using a sorption-enhanced reaction process
dc.typejournal article
dc.type.hasVersionVoR
dc.volume.number331
dspace.entity.typePublication
relation.isAuthorOfPublicatione0f79940-320b-4d89-96b4-700abc44052a
relation.isAuthorOfPublication3e6a9975-23ac-4c3e-b114-bb672a9c06c0
relation.isAuthorOfPublication6d7337b6-a47e-4a09-b249-985fb120b5d2
relation.isAuthorOfPublication1814ebe3-b53d-4917-834d-3bc2e7ca6c7a
relation.isAuthorOfPublication.latestForDiscoverye0f79940-320b-4d89-96b4-700abc44052a
Download
Original bundle
Now showing 1 - 1 of 1
Loading...
Thumbnail Image
Name:
Synthetic natural gas production.pdf
Size:
981.43 KB
Format:
Adobe Portable Document Format
Collections