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...
- 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 https://repositorio.unal.edu.co/bitstream/unal/10253/2/1017125365.2012.pdf.jpg |
bitstream.checksum.fl_str_mv |
b41f011d3a23c08742ee3d19d7a8d64e 1320fb8c6c8da651c5fdd30ca8774fa7 |
bitstream.checksumAlgorithm.fl_str_mv |
MD5 MD5 |
repository.name.fl_str_mv |
Repositorio Institucional Universidad Nacional de Colombia |
repository.mail.fl_str_mv |
repositorio_nal@unal.edu.co |
_version_ |
1814089660424519680 |
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 |