Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2
- Autores
- Cañete, Benjamin; Gigola, Carlos Eugenio; Brignole, Nélida Beatriz
- Año de publicación
- 2014
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- A conceptual design for the production of synthesis gas, suitable for methanol production, is presented. We propose the reforming of natural gas with high CO2 content by using H2O or H2O-O2 as coreactants. A thermodynamic analysis for two reforming processes is developed to get adequate operating conditions for the reformer. The flow scheme for the syngas-methanol plant, together with the corresponding mass balances, is presented. A H2 separation process is considered for syngas composition adjustment. The methanol-loop reactor was also included in the analysis to take into account its close relationship with the reformer's energy balance. For a comparative study, the hypothetical expansion of an existing methanol plant based on steam reforming of natural gas was chosen. A fundamental economic study shows that combined reforming (CO2 + H2O) and tri-reforming (CO2 + H2O+ O2) of CH4 are competitive processes, with lower operating and capital costs in comparison with steam reforming.
Fil: Cañete, Benjamin. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Gigola, Carlos Eugenio. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Brignole, Nélida Beatriz. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina. Universidad Nacional del Sur. Departamento de Ciencias e Ingeniería de la Computación. Laboratorio de Investigación y Desarrollo en Computación Científica; Argentina - Materia
-
Reformado
Reformado Seco
Metanol - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
- Repositorio
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/25795
Ver los metadatos del registro completo
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Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2Cañete, BenjaminGigola, Carlos EugenioBrignole, Nélida BeatrizReformadoReformado SecoMetanolhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2A conceptual design for the production of synthesis gas, suitable for methanol production, is presented. We propose the reforming of natural gas with high CO2 content by using H2O or H2O-O2 as coreactants. A thermodynamic analysis for two reforming processes is developed to get adequate operating conditions for the reformer. The flow scheme for the syngas-methanol plant, together with the corresponding mass balances, is presented. A H2 separation process is considered for syngas composition adjustment. The methanol-loop reactor was also included in the analysis to take into account its close relationship with the reformer's energy balance. For a comparative study, the hypothetical expansion of an existing methanol plant based on steam reforming of natural gas was chosen. A fundamental economic study shows that combined reforming (CO2 + H2O) and tri-reforming (CO2 + H2O+ O2) of CH4 are competitive processes, with lower operating and capital costs in comparison with steam reforming.Fil: Cañete, Benjamin. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaFil: Gigola, Carlos Eugenio. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaFil: Brignole, Nélida Beatriz. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina. Universidad Nacional del Sur. Departamento de Ciencias e Ingeniería de la Computación. Laboratorio de Investigación y Desarrollo en Computación Científica; ArgentinaAmerican Chemical Society2014-04-14info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/25795Cañete, Benjamin; Gigola, Carlos Eugenio; Brignole, Nélida Beatriz; Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2; American Chemical Society; Industrial & Engineering Chemical Research; 53; 17; 14-4-2014; 7103-71120888-58851520-5045CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/doi/10.1021/ie404425einfo:eu-repo/semantics/altIdentifier/url/http://pubs.acs.org/doi/abs/10.1021/ie404425einfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-29T09:36:08Zoai:ri.conicet.gov.ar:11336/25795instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-09-29 09:36:08.903CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
dc.title.none.fl_str_mv |
Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2 |
title |
Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2 |
spellingShingle |
Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2 Cañete, Benjamin Reformado Reformado Seco Metanol |
title_short |
Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2 |
title_full |
Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2 |
title_fullStr |
Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2 |
title_full_unstemmed |
Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2 |
title_sort |
Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2 |
dc.creator.none.fl_str_mv |
Cañete, Benjamin Gigola, Carlos Eugenio Brignole, Nélida Beatriz |
author |
Cañete, Benjamin |
author_facet |
Cañete, Benjamin Gigola, Carlos Eugenio Brignole, Nélida Beatriz |
author_role |
author |
author2 |
Gigola, Carlos Eugenio Brignole, Nélida Beatriz |
author2_role |
author author |
dc.subject.none.fl_str_mv |
Reformado Reformado Seco Metanol |
topic |
Reformado Reformado Seco Metanol |
purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
dc.description.none.fl_txt_mv |
A conceptual design for the production of synthesis gas, suitable for methanol production, is presented. We propose the reforming of natural gas with high CO2 content by using H2O or H2O-O2 as coreactants. A thermodynamic analysis for two reforming processes is developed to get adequate operating conditions for the reformer. The flow scheme for the syngas-methanol plant, together with the corresponding mass balances, is presented. A H2 separation process is considered for syngas composition adjustment. The methanol-loop reactor was also included in the analysis to take into account its close relationship with the reformer's energy balance. For a comparative study, the hypothetical expansion of an existing methanol plant based on steam reforming of natural gas was chosen. A fundamental economic study shows that combined reforming (CO2 + H2O) and tri-reforming (CO2 + H2O+ O2) of CH4 are competitive processes, with lower operating and capital costs in comparison with steam reforming. Fil: Cañete, Benjamin. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina Fil: Gigola, Carlos Eugenio. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina Fil: Brignole, Nélida Beatriz. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina. Universidad Nacional del Sur. Departamento de Ciencias e Ingeniería de la Computación. Laboratorio de Investigación y Desarrollo en Computación Científica; Argentina |
description |
A conceptual design for the production of synthesis gas, suitable for methanol production, is presented. We propose the reforming of natural gas with high CO2 content by using H2O or H2O-O2 as coreactants. A thermodynamic analysis for two reforming processes is developed to get adequate operating conditions for the reformer. The flow scheme for the syngas-methanol plant, together with the corresponding mass balances, is presented. A H2 separation process is considered for syngas composition adjustment. The methanol-loop reactor was also included in the analysis to take into account its close relationship with the reformer's energy balance. For a comparative study, the hypothetical expansion of an existing methanol plant based on steam reforming of natural gas was chosen. A fundamental economic study shows that combined reforming (CO2 + H2O) and tri-reforming (CO2 + H2O+ O2) of CH4 are competitive processes, with lower operating and capital costs in comparison with steam reforming. |
publishDate |
2014 |
dc.date.none.fl_str_mv |
2014-04-14 |
dc.type.none.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion http://purl.org/coar/resource_type/c_6501 info:ar-repo/semantics/articulo |
format |
article |
status_str |
publishedVersion |
dc.identifier.none.fl_str_mv |
http://hdl.handle.net/11336/25795 Cañete, Benjamin; Gigola, Carlos Eugenio; Brignole, Nélida Beatriz; Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2; American Chemical Society; Industrial & Engineering Chemical Research; 53; 17; 14-4-2014; 7103-7112 0888-5885 1520-5045 CONICET Digital CONICET |
url |
http://hdl.handle.net/11336/25795 |
identifier_str_mv |
Cañete, Benjamin; Gigola, Carlos Eugenio; Brignole, Nélida Beatriz; Synthesis gas processes for methanol production via CH4 reforming with CO2, H2O and O2; American Chemical Society; Industrial & Engineering Chemical Research; 53; 17; 14-4-2014; 7103-7112 0888-5885 1520-5045 CONICET Digital CONICET |
dc.language.none.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
info:eu-repo/semantics/altIdentifier/doi/10.1021/ie404425e info:eu-repo/semantics/altIdentifier/url/http://pubs.acs.org/doi/abs/10.1021/ie404425e |
dc.rights.none.fl_str_mv |
info:eu-repo/semantics/openAccess https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
eu_rights_str_mv |
openAccess |
rights_invalid_str_mv |
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
dc.format.none.fl_str_mv |
application/pdf application/pdf application/pdf application/pdf |
dc.publisher.none.fl_str_mv |
American Chemical Society |
publisher.none.fl_str_mv |
American Chemical Society |
dc.source.none.fl_str_mv |
reponame:CONICET Digital (CONICET) instname:Consejo Nacional de Investigaciones Científicas y Técnicas |
reponame_str |
CONICET Digital (CONICET) |
collection |
CONICET Digital (CONICET) |
instname_str |
Consejo Nacional de Investigaciones Científicas y Técnicas |
repository.name.fl_str_mv |
CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas |
repository.mail.fl_str_mv |
dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar |
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1844613131079254016 |
score |
13.070432 |