Optimal renewable production of ammonia from water and air

[EN]n this work a production facility of ammonia has been evaluated using air and water as raw materials. Nitrogen is obtained from air separation using a Linde's double column. Hydrogen is produced from water splitting. Next, hydrogen and oxygen are purified to remove water and traces of chemi...

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Autores: Sánchez García, Antonio, Martín Martín, Mariano
Tipo de recurso: artículo
Estado:Versión enviada para evaluación y publicación
Fecha de publicación:2018
País:España
Institución:Universidad de Salamanca (USAL)
Repositorio:GREDOS. Repositorio Institucional de la Universidad de Salamanca
OAI Identifier:oai:gredos.usal.es:10366/153981
Acceso en línea:http://hdl.handle.net/10366/153981
Access Level:acceso abierto
Palabra clave:Ammonia
Hydrogen
Process optimization
Solar energy
Water
Wind energy
3310.05 Ingeniería de Procesos
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spelling Optimal renewable production of ammonia from water and airSánchez García, AntonioMartín Martín, MarianoAmmoniaHydrogenProcess optimizationSolar energyWaterWind energy3310.05 Ingeniería de Procesos[EN]n this work a production facility of ammonia has been evaluated using air and water as raw materials. Nitrogen is obtained from air separation using a Linde's double column. Hydrogen is produced from water splitting. Next, hydrogen and oxygen are purified to remove water and traces of chemicals. Finally, ammonia is synthesized in a three bed packed reactor. Two cooling designs were considered, indirect and direct cooling. The ammonia is recovered by condensation using the cold air. Power for compression and electrolysis is obtained from renewable sources either solar, photovoltaic, or wind energy. The process is simulated developing surrogate models for each of the units involved with special attention to the electrolyzer, Linde's column, synthesis reactor and ammonia recovery. In particular, the multibed reactor is modeled rigorously off line to validate the conversions and its operation. The full process is formulated as an MINLP problem. Solar energy and indirect cooling are selected for the production of ammonia. However, the high cost of panels results in high investment capital, over 1500 M€, but promising production cost of ammonia, 1.35€/kg.Elsevier202320232018info:eu-repo/semantics/articleinfo:eu-repo/semantics/submittedVersionapplication/pdfhttp://hdl.handle.net/10366/153981reponame:GREDOS. Repositorio Institucional de la Universidad de Salamancainstname:Universidad de Salamanca (USAL)Inglésinfo:eu-repo/semantics/openAccessoai:gredos.usal.es:10366/1539812026-06-07T06:28:51Z
dc.title.none.fl_str_mv Optimal renewable production of ammonia from water and air
title Optimal renewable production of ammonia from water and air
spellingShingle Optimal renewable production of ammonia from water and air
Sánchez García, Antonio
Ammonia
Hydrogen
Process optimization
Solar energy
Water
Wind energy
3310.05 Ingeniería de Procesos
title_short Optimal renewable production of ammonia from water and air
title_full Optimal renewable production of ammonia from water and air
title_fullStr Optimal renewable production of ammonia from water and air
title_full_unstemmed Optimal renewable production of ammonia from water and air
title_sort Optimal renewable production of ammonia from water and air
dc.creator.none.fl_str_mv Sánchez García, Antonio
Martín Martín, Mariano
author Sánchez García, Antonio
author_facet Sánchez García, Antonio
Martín Martín, Mariano
author_role author
author2 Martín Martín, Mariano
author2_role author
dc.subject.none.fl_str_mv Ammonia
Hydrogen
Process optimization
Solar energy
Water
Wind energy
3310.05 Ingeniería de Procesos
topic Ammonia
Hydrogen
Process optimization
Solar energy
Water
Wind energy
3310.05 Ingeniería de Procesos
description [EN]n this work a production facility of ammonia has been evaluated using air and water as raw materials. Nitrogen is obtained from air separation using a Linde's double column. Hydrogen is produced from water splitting. Next, hydrogen and oxygen are purified to remove water and traces of chemicals. Finally, ammonia is synthesized in a three bed packed reactor. Two cooling designs were considered, indirect and direct cooling. The ammonia is recovered by condensation using the cold air. Power for compression and electrolysis is obtained from renewable sources either solar, photovoltaic, or wind energy. The process is simulated developing surrogate models for each of the units involved with special attention to the electrolyzer, Linde's column, synthesis reactor and ammonia recovery. In particular, the multibed reactor is modeled rigorously off line to validate the conversions and its operation. The full process is formulated as an MINLP problem. Solar energy and indirect cooling are selected for the production of ammonia. However, the high cost of panels results in high investment capital, over 1500 M€, but promising production cost of ammonia, 1.35€/kg.
publishDate 2018
dc.date.none.fl_str_mv 2018
2023
2023
dc.type.none.fl_str_mv info:eu-repo/semantics/article
info:eu-repo/semantics/submittedVersion
format article
status_str submittedVersion
dc.identifier.none.fl_str_mv http://hdl.handle.net/10366/153981
url http://hdl.handle.net/10366/153981
dc.language.none.fl_str_mv Inglés
language_invalid_str_mv Inglés
dc.rights.none.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
dc.publisher.none.fl_str_mv Elsevier
publisher.none.fl_str_mv Elsevier
dc.source.none.fl_str_mv reponame:GREDOS. Repositorio Institucional de la Universidad de Salamanca
instname:Universidad de Salamanca (USAL)
instname_str Universidad de Salamanca (USAL)
reponame_str GREDOS. Repositorio Institucional de la Universidad de Salamanca
collection GREDOS. Repositorio Institucional de la Universidad de Salamanca
repository.name.fl_str_mv
repository.mail.fl_str_mv
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