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dc.contributor.authorYáñez Díaz, María
dc.contributor.authorRelvas, Frederico M.
dc.contributor.authorOrtiz Sainz de Aja, Alfredo 
dc.contributor.authorGorri Cirella, Daniel 
dc.contributor.authorMendes, Adélio
dc.contributor.authorOrtiz Uribe, Inmaculada 
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2020-05-19T18:04:05Z
dc.date.available2022-06-02T04:00:23Z
dc.date.issued2020-06-01
dc.identifier.issn1383-5866
dc.identifier.issn1873-3794
dc.identifier.otherCTQ2015-66078-Res_ES
dc.identifier.urihttp://hdl.handle.net/10902/18581
dc.description.abstractIndustrial hydrogen-rich waste streams hold promises in their upgrading to feed fuel cell stacks. As in the ammonia synthesis process, a stream of up to 180–240 Nm3 per ton of ammonia is purged to keep the inert gases concentration below a threshold value; this stream contains large hydrogen quantities, which could be recovered. In the current work, a four-column PSA unit has been used to produce a high-purity hydrogen stream for fuel cell applications from a synthetic mixture with a molar composition of 58% H2, 25% N2, 15% CH4 and 2% Ar, based on ammonia purge gas. Firstly, a comparative performance of four commercially adsorbents was accomplished to obtain the adsorption isotherms of H2, N2, CH4, and Ar, leading to the selection of 5A zeolite adsorbent. Then, the dynamic behavior of a packed bed was studied by single and multicomponent breakthrough experiments and simulated using Aspen Adsorption®. The results, simulations and experimental, indicate that after H2 the first impurity to break thought the column is Ar, followed by N2 and finally by CH4. Then, a design-of-experiments (DoE) methodology was used to select the best operating conditions of the experimental cyclic PSA unit to reach different target hydrogen product concentrations; the overall PSA performance was evaluated in terms of purity and recovery of H2 product. According to the results, the four-column PSA unit running at 9 bar produced a stream with hydrogen concentration of 99.25% and 99.97% of H2, with a recovery of 75.3% and 55.5%, respectively, where the impurities were mostly Ar and N2. In addition to the technical performance, the economic assessment concluded that the cost to compress, transport and purify waste hydrogen to a concentration of 99.97% using a small-scale PSA unit from ammonia plants has been estimated in the range of 1.17–1.39 € kg H2−1, depending on the dispensing pressure of 350 or 700 bar, respectively. These assessments offer a cost-effective solution to produce high-purity H2 as low cost transportation, allowing hydrogen penetration into the mass markets.es_ES
dc.description.sponsorshipThis research was supported by the projects CTQ2015-66078-R (MINECO/FEDER) and SOE1/P1/E0293 (INTERREG SUDOE /FEDER, UE), “Energy Sustainability at the Sudoe Region: Red PEMFC-Sudoe”. Adélio Mendes and Frederico Relvas acknowledge to projects UID/EQU/00511/2019 funded by national funds through FCT/MCTES (PIDDAC); and “LEPABE-2-ECO-INNOVATION” – NORTE‐01‐0145‐FEDER‐000005, funded by Norte Portugal Regional Operational Programme (NORTE 2020), under PORTUGAL 2020 Partnership Agreement, through the European Regional Development Fund (ERDF). Frederico Relvas also acknowledges NORTE-08-5369-FSE-000028 supported by NORTE 2020, under the Portugal 2020 Partnership Agreement and the European Social Fund (ESF).es_ES
dc.format.extent38 p.es_ES
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.rights© 2019. This manuscript version is made available under the CC-BY-NC-ND 4.0 licensees_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.sourceSeparation and Purification Technology, 2020, 240, 116334es_ES
dc.subject.otherHydrogen purificationes_ES
dc.subject.otherAmmonia purge gases_ES
dc.subject.otherPressure swing adsorption (PSA)es_ES
dc.subject.otherZeolite 5Aes_ES
dc.subject.otherAdsorption equilibrium isothermses_ES
dc.titlePSA purification of waste hydrogen from ammonia plants to fuel cell gradees_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publisherVersionhttps://doi.org/10.1016/j.seppur.2019.116334es_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1016/j.seppur.2019.116334
dc.type.versionacceptedVersiones_ES


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© 2019. This manuscript version is made available under the CC-BY-NC-ND 4.0 licenseExcepto si se señala otra cosa, la licencia del ítem se describe como © 2019. This manuscript version is made available under the CC-BY-NC-ND 4.0 license