A model for the prediction of olefin production thermal cracking of light hydrocarbons

Abstract. Thermal cracking of light hydrocarbons is the main route for the production of ethylene and propylene. Associated with cracking there is undesirable coke deposition on the walls of the reactor up to a point in which pressure drop and reduction on heat transfer efficiency are so high that f...

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Autores:
Ramírez Hernández, Astrid Yuliana
Tipo de recurso:
Fecha de publicación:
2012
Institución:
Universidad Nacional de Colombia
Repositorio:
Universidad Nacional de Colombia
Idioma:
spa
OAI Identifier:
oai:repositorio.unal.edu.co:unal/10253
Acceso en línea:
https://repositorio.unal.edu.co/handle/unal/10253
http://bdigital.unal.edu.co/7360/
Palabra clave:
66 Ingeniería química y Tecnologías relacionadas/ Chemical engineering
Light hydrocarbons
Thermal cracking
Olefin production
Coke deposition
Gaseous model
Solid phase model
Hidrocarburos livianos
Craqueo térmico
Deposición de coque
Modelo gaseoso
Modelo gaseoso
Modelo de la fase solida
Rights
openAccess
License
Atribución-NoComercial 4.0 Internacional
id UNACIONAL2_571bb9f5124e974e79632262c6045460
oai_identifier_str oai:repositorio.unal.edu.co:unal/10253
network_acronym_str UNACIONAL2
network_name_str Universidad Nacional de Colombia
repository_id_str
dc.title.spa.fl_str_mv A model for the prediction of olefin production thermal cracking of light hydrocarbons
title A model for the prediction of olefin production thermal cracking of light hydrocarbons
spellingShingle A model for the prediction of olefin production thermal cracking of light hydrocarbons
66 Ingeniería química y Tecnologías relacionadas/ Chemical engineering
Light hydrocarbons
Thermal cracking
Olefin production
Coke deposition
Gaseous model
Solid phase model
Hidrocarburos livianos
Craqueo térmico
Deposición de coque
Modelo gaseoso
Modelo gaseoso
Modelo de la fase solida
title_short A model for the prediction of olefin production thermal cracking of light hydrocarbons
title_full A model for the prediction of olefin production thermal cracking of light hydrocarbons
title_fullStr A model for the prediction of olefin production thermal cracking of light hydrocarbons
title_full_unstemmed A model for the prediction of olefin production thermal cracking of light hydrocarbons
title_sort A model for the prediction of olefin production thermal cracking of light hydrocarbons
dc.creator.fl_str_mv Ramírez Hernández, Astrid Yuliana
dc.contributor.advisor.spa.fl_str_mv Molina, Alejandro (Thesis advisor)
dc.contributor.author.spa.fl_str_mv Ramírez Hernández, Astrid Yuliana
dc.subject.ddc.spa.fl_str_mv 66 Ingeniería química y Tecnologías relacionadas/ Chemical engineering
topic 66 Ingeniería química y Tecnologías relacionadas/ Chemical engineering
Light hydrocarbons
Thermal cracking
Olefin production
Coke deposition
Gaseous model
Solid phase model
Hidrocarburos livianos
Craqueo térmico
Deposición de coque
Modelo gaseoso
Modelo gaseoso
Modelo de la fase solida
dc.subject.proposal.spa.fl_str_mv Light hydrocarbons
Thermal cracking
Olefin production
Coke deposition
Gaseous model
Solid phase model
Hidrocarburos livianos
Craqueo térmico
Deposición de coque
Modelo gaseoso
Modelo gaseoso
Modelo de la fase solida
description Abstract. Thermal cracking of light hydrocarbons is the main route for the production of ethylene and propylene. Associated with cracking there is undesirable coke deposition on the walls of the reactor up to a point in which pressure drop and reduction on heat transfer efficiency are so high that furnace maintenance stops are mandatory. Predictions of diameter reduction because of coke deposition for two different raw materials (ethane and 50% ethane/propane mixture) were conducted with a pyrolysis reactor model developed to this aim. The cracking reactor was modeled as a tubular, one-dimensional reactor. After a careful evaluation of the kinetic mechanisms available in the literature for hydrocarbon pyrolysis, the mechanism that yielded results that were closer to those expected for ethane conversion in an industrial furnace was selected. A mechanism for coke formation, that has as input the species concentrations predicted by the gas phase mechanism, was proposed. The solid phase mechanism considers the most important precursors (benzene and acetylene) for the formation of carbonaceous materials (such as soot and coke) that the state of the art reports and was calibrated based on industrial data and with the predicted concentration profile of benzene. According to the model for the cracking reactor evaluated in this research, the reduction in the diameter is 30% higher when the raw material of the reactor changes from ethane to a mixture of 50%ethane/50%propane
publishDate 2012
dc.date.issued.spa.fl_str_mv 2012
dc.date.accessioned.spa.fl_str_mv 2019-06-24T23:32:52Z
dc.date.available.spa.fl_str_mv 2019-06-24T23:32:52Z
dc.type.spa.fl_str_mv Trabajo de grado - Maestría
dc.type.driver.spa.fl_str_mv info:eu-repo/semantics/masterThesis
dc.type.version.spa.fl_str_mv info:eu-repo/semantics/acceptedVersion
dc.type.content.spa.fl_str_mv Text
dc.type.redcol.spa.fl_str_mv http://purl.org/redcol/resource_type/TM
status_str acceptedVersion
dc.identifier.uri.none.fl_str_mv https://repositorio.unal.edu.co/handle/unal/10253
dc.identifier.eprints.spa.fl_str_mv http://bdigital.unal.edu.co/7360/
url https://repositorio.unal.edu.co/handle/unal/10253
http://bdigital.unal.edu.co/7360/
dc.language.iso.spa.fl_str_mv spa
language spa
dc.relation.ispartof.spa.fl_str_mv Universidad Nacional de Colombia Sede Medellín Facultad de Minas Escuela de Procesos y Energía
Escuela de Procesos y Energía
dc.relation.references.spa.fl_str_mv Ramírez Hernández, Astrid Yuliana (2012) A model for the prediction of olefin production thermal cracking of light hydrocarbons. Maestría thesis, Universidad Nacional de Colombia, Sede Medellín.
dc.rights.spa.fl_str_mv Derechos reservados - Universidad Nacional de Colombia
dc.rights.coar.fl_str_mv http://purl.org/coar/access_right/c_abf2
dc.rights.license.spa.fl_str_mv Atribución-NoComercial 4.0 Internacional
dc.rights.uri.spa.fl_str_mv http://creativecommons.org/licenses/by-nc/4.0/
dc.rights.accessrights.spa.fl_str_mv info:eu-repo/semantics/openAccess
rights_invalid_str_mv Atribución-NoComercial 4.0 Internacional
Derechos reservados - Universidad Nacional de Colombia
http://creativecommons.org/licenses/by-nc/4.0/
http://purl.org/coar/access_right/c_abf2
eu_rights_str_mv openAccess
dc.format.mimetype.spa.fl_str_mv application/pdf
institution Universidad Nacional de Colombia
bitstream.url.fl_str_mv https://repositorio.unal.edu.co/bitstream/unal/10253/1/1017125365.2012.pdf
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repository.name.fl_str_mv Repositorio Institucional Universidad Nacional de Colombia
repository.mail.fl_str_mv repositorio_nal@unal.edu.co
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spelling Atribución-NoComercial 4.0 InternacionalDerechos reservados - Universidad Nacional de Colombiahttp://creativecommons.org/licenses/by-nc/4.0/info:eu-repo/semantics/openAccesshttp://purl.org/coar/access_right/c_abf2Molina, Alejandro (Thesis advisor)6d7e82ac-22a7-4709-8bd7-4f410c91cd66-1Ramírez Hernández, Astrid Yuliana71cd6f1c-576b-43c3-89e9-8c4661c7c0d63002019-06-24T23:32:52Z2019-06-24T23:32:52Z2012https://repositorio.unal.edu.co/handle/unal/10253http://bdigital.unal.edu.co/7360/Abstract. Thermal cracking of light hydrocarbons is the main route for the production of ethylene and propylene. Associated with cracking there is undesirable coke deposition on the walls of the reactor up to a point in which pressure drop and reduction on heat transfer efficiency are so high that furnace maintenance stops are mandatory. Predictions of diameter reduction because of coke deposition for two different raw materials (ethane and 50% ethane/propane mixture) were conducted with a pyrolysis reactor model developed to this aim. The cracking reactor was modeled as a tubular, one-dimensional reactor. After a careful evaluation of the kinetic mechanisms available in the literature for hydrocarbon pyrolysis, the mechanism that yielded results that were closer to those expected for ethane conversion in an industrial furnace was selected. A mechanism for coke formation, that has as input the species concentrations predicted by the gas phase mechanism, was proposed. The solid phase mechanism considers the most important precursors (benzene and acetylene) for the formation of carbonaceous materials (such as soot and coke) that the state of the art reports and was calibrated based on industrial data and with the predicted concentration profile of benzene. According to the model for the cracking reactor evaluated in this research, the reduction in the diameter is 30% higher when the raw material of the reactor changes from ethane to a mixture of 50%ethane/50%propaneResumen: El craqueo térmico de hidrocarburos livianos es la principal ruta para la producción de etileno y propileno. Asociado con las reacciones de pirolisis, hay una deposición de coque en las paredes del serpentín indeseada, la cual incrementa con el tiempo hasta llegar a un punto en que la caída de presión a lo largo del serpentín y la reducción en la eficiencia de la transferencia de calor son tan altas que se hace necesario hacer una parada de mantenimiento en el proceso. Se predijo la reducción en el diámetro del reactor para dos materias primas (etano y una mezcla 50% etano/propano) mediante un modelo que se desarrolló con ese fin. El reactor se simuló como un tubular y en una dimensión. Luego de una revisión cuidadosa de los mecanismos disponibles en la literatura para la pirólisis de hidrocarburos, se seleccionó aquel que entregó predicciones más cercanas a las de un horno industrial. Se propuso un mecanismo para la formación de coque que toma como datos de entrada la concentración en de precursores de acuerdo con el mecanismo de fase gaseosa. El mecanismo para la fase sólida considera los principales precursores (benceno y acetileno) para la formación de materiales carbonosos (como hollín y coque) que el estado del arte reporta y se calibró con IIbase en datos industriales y con el perfil de concentración de benceno. Según el modelo, para el reactor de craqueo térmico que se estudia en esta investigación, la reducción de diámetro es 30% más alta cuando la materia prima del reactor cambia de etano a una mezcla 50% etano/propano.Maestríaapplication/pdfspaUniversidad Nacional de Colombia Sede Medellín Facultad de Minas Escuela de Procesos y EnergíaEscuela de Procesos y EnergíaRamírez Hernández, Astrid Yuliana (2012) A model for the prediction of olefin production thermal cracking of light hydrocarbons. Maestría thesis, Universidad Nacional de Colombia, Sede Medellín.66 Ingeniería química y Tecnologías relacionadas/ Chemical engineeringLight hydrocarbonsThermal crackingOlefin productionCoke depositionGaseous modelSolid phase modelHidrocarburos livianosCraqueo térmicoDeposición de coqueModelo gaseosoModelo gaseosoModelo de la fase solidaA model for the prediction of olefin production thermal cracking of light hydrocarbonsTrabajo de grado - Maestríainfo:eu-repo/semantics/masterThesisinfo:eu-repo/semantics/acceptedVersionTexthttp://purl.org/redcol/resource_type/TMORIGINAL1017125365.2012.pdfTesis de Maestría en Ingeniería - Ingeniería Químicaapplication/pdf679099https://repositorio.unal.edu.co/bitstream/unal/10253/1/1017125365.2012.pdfb41f011d3a23c08742ee3d19d7a8d64eMD51THUMBNAIL1017125365.2012.pdf.jpg1017125365.2012.pdf.jpgGenerated Thumbnailimage/jpeg4145https://repositorio.unal.edu.co/bitstream/unal/10253/2/1017125365.2012.pdf.jpg1320fb8c6c8da651c5fdd30ca8774fa7MD52unal/10253oai:repositorio.unal.edu.co:unal/102532023-10-09 21:03:02.213Repositorio Institucional Universidad Nacional de Colombiarepositorio_nal@unal.edu.co