Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling
- Autores
- Bastos, Tecio Santos; Rodriguez Reartes, Sabrina Belen; Zabaloy, Marcelo Santiago; Cassaro, Rafael; Bazito Camino, Reinaldo; Borges Rodrigues, Gustavo; Dariva, Cláudio; Franceschi, Elton
- Año de publicación
- 2019
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- The experimental study and thermodynamic modeling of the phase behavior of pressurized reactional systems allows the optimization of several unit operations involved in the process of product formation. In this work, experimental data of phase equilibria for the CO 2 + p-nitrobenzaldheyde binary system were obtained through the static synthetic method. The range of temperature, pressure, and p-nitrobenzaldehyde molar fraction investigated were 281-353 K, 6.5-25.0 MPa, and 2.638 × 10 -3 to 5.903 × 10 -3 , respectively. A model previously developed to describe asymmetric mixtures presenting fluid and solid phases was applied to describe the phase behavior of the system. This model uses the Peng-Robinson equation of state (PR-EoS) to describe the properties of the fluid phases and an expression for the fugacity of p-nitrobenzaldehyde as a pure solid for the solid phase. Different model parametrization strategies were studied, and complete isopleths were calculated considering the fluid-fluid, solid-fluid, and solid-fluid-fluid phase equilibria over wide ranges of temperature and pressure. The experimental results showed nonmonotonic (local minimum) solid-fluid phase behavior for all mixture compositions investigated. The model employed and the parametrization strategies were able to describe the experimentally observed phase behavior.
Fil: Bastos, Tecio Santos. Universidade Tiradentes; Brasil
Fil: Rodriguez Reartes, Sabrina Belen. 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: Zabaloy, Marcelo Santiago. 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: Cassaro, Rafael. Universidade de Sao Paulo; Brasil
Fil: Bazito Camino, Reinaldo. Universidade de Sao Paulo; Brasil
Fil: Borges Rodrigues, Gustavo. Institute Of Technology And Research ; China. Universidade Tiradentes; Brasil
Fil: Dariva, Cláudio. Universidade Tiradentes; Brasil. Institute Of Technology And Research ; China
Fil: Franceschi, Elton. Universidade Tiradentes; Brasil. Institute Of Technology And Research ; China - Materia
-
Carbon Dioxide
p-Nitrobenzaldehyde
SOLID-FLUID EQUILIBRIUM - 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:11336/115976
Ver los metadatos del registro completo
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CONICET Digital (CONICET) |
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Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and ModelingBastos, Tecio SantosRodriguez Reartes, Sabrina BelenZabaloy, Marcelo SantiagoCassaro, RafaelBazito Camino, ReinaldoBorges Rodrigues, GustavoDariva, CláudioFranceschi, EltonCarbon Dioxidep-NitrobenzaldehydeSOLID-FLUID EQUILIBRIUMhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2The experimental study and thermodynamic modeling of the phase behavior of pressurized reactional systems allows the optimization of several unit operations involved in the process of product formation. In this work, experimental data of phase equilibria for the CO 2 + p-nitrobenzaldheyde binary system were obtained through the static synthetic method. The range of temperature, pressure, and p-nitrobenzaldehyde molar fraction investigated were 281-353 K, 6.5-25.0 MPa, and 2.638 × 10 -3 to 5.903 × 10 -3 , respectively. A model previously developed to describe asymmetric mixtures presenting fluid and solid phases was applied to describe the phase behavior of the system. This model uses the Peng-Robinson equation of state (PR-EoS) to describe the properties of the fluid phases and an expression for the fugacity of p-nitrobenzaldehyde as a pure solid for the solid phase. Different model parametrization strategies were studied, and complete isopleths were calculated considering the fluid-fluid, solid-fluid, and solid-fluid-fluid phase equilibria over wide ranges of temperature and pressure. The experimental results showed nonmonotonic (local minimum) solid-fluid phase behavior for all mixture compositions investigated. The model employed and the parametrization strategies were able to describe the experimentally observed phase behavior.Fil: Bastos, Tecio Santos. Universidade Tiradentes; BrasilFil: Rodriguez Reartes, Sabrina Belen. 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: Zabaloy, Marcelo Santiago. 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: Cassaro, Rafael. Universidade de Sao Paulo; BrasilFil: Bazito Camino, Reinaldo. Universidade de Sao Paulo; BrasilFil: Borges Rodrigues, Gustavo. Institute Of Technology And Research ; China. Universidade Tiradentes; BrasilFil: Dariva, Cláudio. Universidade Tiradentes; Brasil. Institute Of Technology And Research ; ChinaFil: Franceschi, Elton. Universidade Tiradentes; Brasil. Institute Of Technology And Research ; ChinaAmerican Chemical Society2019-03-11info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/115976Bastos, Tecio Santos; Rodriguez Reartes, Sabrina Belen; Zabaloy, Marcelo Santiago; Cassaro, Rafael; Bazito Camino, Reinaldo; et al.; Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling; American Chemical Society; Journal of Chemical and Engineering Data; 64; 5; 11-3-2019; 2116-21250021-95681520-5134CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/doi/10.1021/acs.jced.8b01067info:eu-repo/semantics/altIdentifier/url/https://pubs.acs.org/doi/10.1021/acs.jced.8b01067info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-03T10:04:44Zoai:ri.conicet.gov.ar:11336/115976instacron: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:34982025-09-03 10:04:44.516CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
dc.title.none.fl_str_mv |
Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling |
title |
Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling |
spellingShingle |
Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling Bastos, Tecio Santos Carbon Dioxide p-Nitrobenzaldehyde SOLID-FLUID EQUILIBRIUM |
title_short |
Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling |
title_full |
Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling |
title_fullStr |
Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling |
title_full_unstemmed |
Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling |
title_sort |
Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling |
dc.creator.none.fl_str_mv |
Bastos, Tecio Santos Rodriguez Reartes, Sabrina Belen Zabaloy, Marcelo Santiago Cassaro, Rafael Bazito Camino, Reinaldo Borges Rodrigues, Gustavo Dariva, Cláudio Franceschi, Elton |
author |
Bastos, Tecio Santos |
author_facet |
Bastos, Tecio Santos Rodriguez Reartes, Sabrina Belen Zabaloy, Marcelo Santiago Cassaro, Rafael Bazito Camino, Reinaldo Borges Rodrigues, Gustavo Dariva, Cláudio Franceschi, Elton |
author_role |
author |
author2 |
Rodriguez Reartes, Sabrina Belen Zabaloy, Marcelo Santiago Cassaro, Rafael Bazito Camino, Reinaldo Borges Rodrigues, Gustavo Dariva, Cláudio Franceschi, Elton |
author2_role |
author author author author author author author |
dc.subject.none.fl_str_mv |
Carbon Dioxide p-Nitrobenzaldehyde SOLID-FLUID EQUILIBRIUM |
topic |
Carbon Dioxide p-Nitrobenzaldehyde SOLID-FLUID EQUILIBRIUM |
purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
dc.description.none.fl_txt_mv |
The experimental study and thermodynamic modeling of the phase behavior of pressurized reactional systems allows the optimization of several unit operations involved in the process of product formation. In this work, experimental data of phase equilibria for the CO 2 + p-nitrobenzaldheyde binary system were obtained through the static synthetic method. The range of temperature, pressure, and p-nitrobenzaldehyde molar fraction investigated were 281-353 K, 6.5-25.0 MPa, and 2.638 × 10 -3 to 5.903 × 10 -3 , respectively. A model previously developed to describe asymmetric mixtures presenting fluid and solid phases was applied to describe the phase behavior of the system. This model uses the Peng-Robinson equation of state (PR-EoS) to describe the properties of the fluid phases and an expression for the fugacity of p-nitrobenzaldehyde as a pure solid for the solid phase. Different model parametrization strategies were studied, and complete isopleths were calculated considering the fluid-fluid, solid-fluid, and solid-fluid-fluid phase equilibria over wide ranges of temperature and pressure. The experimental results showed nonmonotonic (local minimum) solid-fluid phase behavior for all mixture compositions investigated. The model employed and the parametrization strategies were able to describe the experimentally observed phase behavior. Fil: Bastos, Tecio Santos. Universidade Tiradentes; Brasil Fil: Rodriguez Reartes, Sabrina Belen. 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: Zabaloy, Marcelo Santiago. 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: Cassaro, Rafael. Universidade de Sao Paulo; Brasil Fil: Bazito Camino, Reinaldo. Universidade de Sao Paulo; Brasil Fil: Borges Rodrigues, Gustavo. Institute Of Technology And Research ; China. Universidade Tiradentes; Brasil Fil: Dariva, Cláudio. Universidade Tiradentes; Brasil. Institute Of Technology And Research ; China Fil: Franceschi, Elton. Universidade Tiradentes; Brasil. Institute Of Technology And Research ; China |
description |
The experimental study and thermodynamic modeling of the phase behavior of pressurized reactional systems allows the optimization of several unit operations involved in the process of product formation. In this work, experimental data of phase equilibria for the CO 2 + p-nitrobenzaldheyde binary system were obtained through the static synthetic method. The range of temperature, pressure, and p-nitrobenzaldehyde molar fraction investigated were 281-353 K, 6.5-25.0 MPa, and 2.638 × 10 -3 to 5.903 × 10 -3 , respectively. A model previously developed to describe asymmetric mixtures presenting fluid and solid phases was applied to describe the phase behavior of the system. This model uses the Peng-Robinson equation of state (PR-EoS) to describe the properties of the fluid phases and an expression for the fugacity of p-nitrobenzaldehyde as a pure solid for the solid phase. Different model parametrization strategies were studied, and complete isopleths were calculated considering the fluid-fluid, solid-fluid, and solid-fluid-fluid phase equilibria over wide ranges of temperature and pressure. The experimental results showed nonmonotonic (local minimum) solid-fluid phase behavior for all mixture compositions investigated. The model employed and the parametrization strategies were able to describe the experimentally observed phase behavior. |
publishDate |
2019 |
dc.date.none.fl_str_mv |
2019-03-11 |
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/11336/115976 Bastos, Tecio Santos; Rodriguez Reartes, Sabrina Belen; Zabaloy, Marcelo Santiago; Cassaro, Rafael; Bazito Camino, Reinaldo; et al.; Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling; American Chemical Society; Journal of Chemical and Engineering Data; 64; 5; 11-3-2019; 2116-2125 0021-9568 1520-5134 CONICET Digital CONICET |
url |
http://hdl.handle.net/11336/115976 |
identifier_str_mv |
Bastos, Tecio Santos; Rodriguez Reartes, Sabrina Belen; Zabaloy, Marcelo Santiago; Cassaro, Rafael; Bazito Camino, Reinaldo; et al.; Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling; American Chemical Society; Journal of Chemical and Engineering Data; 64; 5; 11-3-2019; 2116-2125 0021-9568 1520-5134 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/acs.jced.8b01067 info:eu-repo/semantics/altIdentifier/url/https://pubs.acs.org/doi/10.1021/acs.jced.8b01067 |
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 |
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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1842269872907616256 |
score |
13.13397 |