Purification of the carbon dioxide emitted by gas treatment plants

In natural gas plants, the carbon dioxide (CO2) traveling in the extracted stream is separated and released to the atmosphere. This stream also contains hydrogen sulfide (H2S), water and hydrocarbons. The purpose of this investigation was to design a process to purify this CO2 stream, to it...

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Tipo de recurso:
Fecha de publicación:
2018
Institución:
Universidad Pedagógica y Tecnológica de Colombia
Repositorio:
RiUPTC: Repositorio Institucional UPTC
Idioma:
spa
OAI Identifier:
oai:repositorio.uptc.edu.co:001/15240
Acceso en línea:
https://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/7392
https://repositorio.uptc.edu.co/handle/001/15240
Palabra clave:
Calentamiento global
CAPEX
Costos de inversión
Captura y uso de carbono
Simulación de procesos.
Global warming; CAPEX; Capital expenses; Carbon capture and utilization (CCU); Process simulation
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License
Derechos de autor 2018 CIENCIA EN DESARROLLO
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spelling 2018-07-042024-07-08T14:23:54Z2024-07-08T14:23:54Zhttps://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/739210.19053/01217488.v9.n2.2018.7392https://repositorio.uptc.edu.co/handle/001/15240In natural gas plants, the carbon dioxide (CO2) traveling in the extracted stream is separated and released to the atmosphere. This stream also contains hydrogen sulfide (H2S), water and hydrocarbons. The purpose of this investigation was to design a process to purify this CO2 stream, to its further use in the food industry. There, the CO2 can be employed in carbonated drinks and as supercritical fluid; requiring a purity higher than 99.95 mol%. Therefore, a real flow of 3454 ton/year CO2 was selected as case of study, which is emitted in a gas treatment plant located in Neiva, Colombia. This stream was simulated in ProMax and subjected to chemical absorption with methyl diethanolamine (MDEA), to a dehydration with diethylene glycol combined with molécular sieve, to a Ryan-Holmes cryogenic process for removing light components (methane and ethane) and their combinations. The combination of the three processes allowed us for a 99.95% CO2 recovery and a 99.99 mol% CO2 purity, requiring capital expenses (CAPEX) of USD 412.323 or 53 USD/tCO2. This CO2 could be commercialized at sell prices as high as 5000 USD/tCO2 to the food industry. In addition, the combination of the two first processes delivered a CAPEX of 37 USD/tCO2 with a 99.85 mol% CO2 purity, suitable for other applications requiring less purity in the food industry or improved oil recovery.En las plantas de extracción de gas natural (GN), el dióxido de carbono (CO2) que viaja en la corriente extraída se separa y se libera a la atmósfera, acompañado de ácido sulfídrico (H2S), agua e hidrocarburos. El objetivo de esta investigación fue diseñar un proceso para purificar esta corriente de CO2, para su posterior uso en la industria alimenticia, donde el CO2 se puede usar en bebidas carbonatadas y como fluido supercrítico; requiriendo una pureza superior a 99,95% mol. Para ello, se seleccionó como caso de estudio un flujo real de 3454 ton/año de CO2 emitido por una planta de gas natural localizada en Neiva, Colombia y se simuló en ProMax. Se simularon la absorción química con metildietanolamina (MDEA), deshidratación con trietilenglicol (TEG) combinada con tamiz molecular, procesos criogénicos de Ryan Holmes y sus combinaciones. La combinación de los tres procesos permitió una recuperación de 99,95% de CO2 con una pureza del 99,99 %mol, requiriendo una inversión total de USD 412.323 o 53 USD/tCO2. Esta CO2 podría ser comercializado a valores superiores a 5000 USD/tCO2 para la industria alimenticia. Además, la combinación de los dos primeros procesos arrojó costos de 37 USD/tCO2, produciendo una pureza de CO2 de 99,85 %mol apto para otras aplicaciones.application/pdfspaspaUniversidad Pedagógica y Tecnológica de Colombiahttps://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/7392/7266Derechos de autor 2018 CIENCIA EN DESARROLLOhttp://purl.org/coar/access_right/c_abf2Ciencia En Desarrollo; Vol. 9 No. 2 (2018): Vol 9, Núm. 2 (2018): Vol 9, Núm 2(2018): Julio- Diciembre; 137-148Ciencia en Desarrollo; Vol. 9 Núm. 2 (2018): Vol 9, Núm. 2 (2018): Vol 9, Núm 2(2018): Julio- Diciembre; 137-1482462-76580121-7488Calentamiento globalCAPEXCostos de inversiónCaptura y uso de carbonoSimulación de procesos.Global warming; CAPEX; Capital expenses; Carbon capture and utilization (CCU); Process simulationPurification of the carbon dioxide emitted by gas treatment plantsPurificación de dióxido de carbono emitido en las plantas de gas naturalinfo:eu-repo/semantics/articleSimulación de procesoshttp://purl.org/coar/version/c_970fb48d4fbd8a85http://purl.org/coar/resource_type/c_2df8fbb1Gámez, NancyCobo, Martha001/15240oai:repositorio.uptc.edu.co:001/152402025-07-18 10:56:40.337metadata.onlyhttps://repositorio.uptc.edu.coRepositorio Institucional UPTCrepositorio.uptc@uptc.edu.co
dc.title.en-US.fl_str_mv Purification of the carbon dioxide emitted by gas treatment plants
dc.title.es-ES.fl_str_mv Purificación de dióxido de carbono emitido en las plantas de gas natural
title Purification of the carbon dioxide emitted by gas treatment plants
spellingShingle Purification of the carbon dioxide emitted by gas treatment plants
Calentamiento global
CAPEX
Costos de inversión
Captura y uso de carbono
Simulación de procesos.
Global warming; CAPEX; Capital expenses; Carbon capture and utilization (CCU); Process simulation
title_short Purification of the carbon dioxide emitted by gas treatment plants
title_full Purification of the carbon dioxide emitted by gas treatment plants
title_fullStr Purification of the carbon dioxide emitted by gas treatment plants
title_full_unstemmed Purification of the carbon dioxide emitted by gas treatment plants
title_sort Purification of the carbon dioxide emitted by gas treatment plants
dc.subject.es-ES.fl_str_mv Calentamiento global
CAPEX
Costos de inversión
Captura y uso de carbono
Simulación de procesos.
topic Calentamiento global
CAPEX
Costos de inversión
Captura y uso de carbono
Simulación de procesos.
Global warming; CAPEX; Capital expenses; Carbon capture and utilization (CCU); Process simulation
dc.subject.en-US.fl_str_mv Global warming; CAPEX; Capital expenses; Carbon capture and utilization (CCU); Process simulation
description In natural gas plants, the carbon dioxide (CO2) traveling in the extracted stream is separated and released to the atmosphere. This stream also contains hydrogen sulfide (H2S), water and hydrocarbons. The purpose of this investigation was to design a process to purify this CO2 stream, to its further use in the food industry. There, the CO2 can be employed in carbonated drinks and as supercritical fluid; requiring a purity higher than 99.95 mol%. Therefore, a real flow of 3454 ton/year CO2 was selected as case of study, which is emitted in a gas treatment plant located in Neiva, Colombia. This stream was simulated in ProMax and subjected to chemical absorption with methyl diethanolamine (MDEA), to a dehydration with diethylene glycol combined with molécular sieve, to a Ryan-Holmes cryogenic process for removing light components (methane and ethane) and their combinations. The combination of the three processes allowed us for a 99.95% CO2 recovery and a 99.99 mol% CO2 purity, requiring capital expenses (CAPEX) of USD 412.323 or 53 USD/tCO2. This CO2 could be commercialized at sell prices as high as 5000 USD/tCO2 to the food industry. In addition, the combination of the two first processes delivered a CAPEX of 37 USD/tCO2 with a 99.85 mol% CO2 purity, suitable for other applications requiring less purity in the food industry or improved oil recovery.
publishDate 2018
dc.date.accessioned.none.fl_str_mv 2024-07-08T14:23:54Z
dc.date.available.none.fl_str_mv 2024-07-08T14:23:54Z
dc.date.none.fl_str_mv 2018-07-04
dc.type.none.fl_str_mv info:eu-repo/semantics/article
dc.type.es-ES.fl_str_mv Simulación de procesos
dc.type.coarversion.fl_str_mv http://purl.org/coar/version/c_970fb48d4fbd8a85
dc.type.coar.fl_str_mv http://purl.org/coar/resource_type/c_2df8fbb1
dc.identifier.none.fl_str_mv https://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/7392
10.19053/01217488.v9.n2.2018.7392
dc.identifier.uri.none.fl_str_mv https://repositorio.uptc.edu.co/handle/001/15240
url https://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/7392
https://repositorio.uptc.edu.co/handle/001/15240
identifier_str_mv 10.19053/01217488.v9.n2.2018.7392
dc.language.none.fl_str_mv spa
dc.language.iso.none.fl_str_mv spa
language spa
dc.relation.none.fl_str_mv https://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/7392/7266
dc.rights.es-ES.fl_str_mv Derechos de autor 2018 CIENCIA EN DESARROLLO
dc.rights.coar.fl_str_mv http://purl.org/coar/access_right/c_abf2
rights_invalid_str_mv Derechos de autor 2018 CIENCIA EN DESARROLLO
http://purl.org/coar/access_right/c_abf2
dc.format.none.fl_str_mv application/pdf
dc.publisher.es-ES.fl_str_mv Universidad Pedagógica y Tecnológica de Colombia
dc.source.en-US.fl_str_mv Ciencia En Desarrollo; Vol. 9 No. 2 (2018): Vol 9, Núm. 2 (2018): Vol 9, Núm 2(2018): Julio- Diciembre; 137-148
dc.source.es-ES.fl_str_mv Ciencia en Desarrollo; Vol. 9 Núm. 2 (2018): Vol 9, Núm. 2 (2018): Vol 9, Núm 2(2018): Julio- Diciembre; 137-148
dc.source.none.fl_str_mv 2462-7658
0121-7488
institution Universidad Pedagógica y Tecnológica de Colombia
repository.name.fl_str_mv Repositorio Institucional UPTC
repository.mail.fl_str_mv repositorio.uptc@uptc.edu.co
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