The corrosion process of p-110 steel in stimulation fluids used in the oil industry

ABSTRACT: The use of chelating agents in the oil well stimulation processes has been proposed as an alternative to the acid treatment when the formations damage do not allow the usage of strong chemical attack. However, this procedure can arouse the corrosion of the steel used in the infrastructure...

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Autores:
Calderón Gutiérrez, Jorge Andrés
Bonilla Muñetones, Gloria Fernanda
Carreño, Javier Alejandro
Tipo de recurso:
Article of investigation
Fecha de publicación:
2014
Institución:
Universidad de Antioquia
Repositorio:
Repositorio UdeA
Idioma:
eng
OAI Identifier:
oai:bibliotecadigital.udea.edu.co:10495/36319
Acceso en línea:
https://hdl.handle.net/10495/36319
http://www.scielo.org.co/pdf/ctyf/v5n4/v5n4a03.pdf
Palabra clave:
Ácido Edético
Edetic Acid
Recursos petroleros
Petroleum resources
Corrosión
Corrosion
Electrochemical techniques
Metal dissolution
http://vocabularies.unesco.org/thesaurus/concept14587
http://vocabularies.unesco.org/thesaurus/concept5010
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openAccess
License
http://creativecommons.org/licenses/by-nc-sa/2.5/co/
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dc.title.spa.fl_str_mv The corrosion process of p-110 steel in stimulation fluids used in the oil industry
dc.title.translated.spa.fl_str_mv El proceso de corrosión del acero p-110 en fluidos de estimulación utilizados en la industria del petróleo
title The corrosion process of p-110 steel in stimulation fluids used in the oil industry
spellingShingle The corrosion process of p-110 steel in stimulation fluids used in the oil industry
Ácido Edético
Edetic Acid
Recursos petroleros
Petroleum resources
Corrosión
Corrosion
Electrochemical techniques
Metal dissolution
http://vocabularies.unesco.org/thesaurus/concept14587
http://vocabularies.unesco.org/thesaurus/concept5010
title_short The corrosion process of p-110 steel in stimulation fluids used in the oil industry
title_full The corrosion process of p-110 steel in stimulation fluids used in the oil industry
title_fullStr The corrosion process of p-110 steel in stimulation fluids used in the oil industry
title_full_unstemmed The corrosion process of p-110 steel in stimulation fluids used in the oil industry
title_sort The corrosion process of p-110 steel in stimulation fluids used in the oil industry
dc.creator.fl_str_mv Calderón Gutiérrez, Jorge Andrés
Bonilla Muñetones, Gloria Fernanda
Carreño, Javier Alejandro
dc.contributor.author.none.fl_str_mv Calderón Gutiérrez, Jorge Andrés
Bonilla Muñetones, Gloria Fernanda
Carreño, Javier Alejandro
dc.contributor.researchgroup.spa.fl_str_mv Centro de Investigación Innovación y Desarrollo de Materiales (CIDEMAT)
dc.subject.decs.none.fl_str_mv Ácido Edético
Edetic Acid
topic Ácido Edético
Edetic Acid
Recursos petroleros
Petroleum resources
Corrosión
Corrosion
Electrochemical techniques
Metal dissolution
http://vocabularies.unesco.org/thesaurus/concept14587
http://vocabularies.unesco.org/thesaurus/concept5010
dc.subject.unesco.none.fl_str_mv Recursos petroleros
Petroleum resources
Corrosión
Corrosion
dc.subject.proposal.spa.fl_str_mv Electrochemical techniques
Metal dissolution
dc.subject.unescouri.none.fl_str_mv http://vocabularies.unesco.org/thesaurus/concept14587
http://vocabularies.unesco.org/thesaurus/concept5010
description ABSTRACT: The use of chelating agents in the oil well stimulation processes has been proposed as an alternative to the acid treatment when the formations damage do not allow the usage of strong chemical attack. However, this procedure can arouse the corrosion of the steel used in the infrastructure of the oil production. In this study, the corrosion kinetics of the P-110 steel in ethylenediaminetetraacetic acid (EDTA) based fluids is assessed under different conditions of evaluation. Linear polarization was performed in different hydrodynamic regimes and at different temperatures, in order to evaluate the kinetic of steel corrosion. The working electrolyte solution comprises 10% disodium EDTA and 20% tetrasodium EDTA. The increase of temperature from 25 to 80°C in both electrolytes increments the corrosion rate of steel in at least one order of magnitude; particularly in EDTA-Na2 solutions. Corrosion rates of 0.29x101 and 1.67x102 mm·y-1 were measured at 25 and 80°C, respectively. The hydrodynamic regime plays an important role in the corrosion of steel only in the disodium solution, where corrosion rates were increased at higher rotation speeds of the electrode. The cathodic depolarization effect is more important in the EDTA-Na2 than in the EDTA-Na4 solution, making it more corrosive.
publishDate 2014
dc.date.issued.none.fl_str_mv 2014
dc.date.accessioned.none.fl_str_mv 2023-08-22T20:29:39Z
dc.date.available.none.fl_str_mv 2023-08-22T20:29:39Z
dc.type.spa.fl_str_mv Artículo de investigación
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dc.identifier.citation.spa.fl_str_mv Calderón, J. A., Bonilla, G. F. & Carreño, J. A. (2014). The corrosion process of P-110 steel in stimulation fluids used in the oil industry. CT&F - Ciencia, Tecnología y Futuro, 5(4), 35-48
dc.identifier.issn.none.fl_str_mv 0122-5383
dc.identifier.uri.none.fl_str_mv https://hdl.handle.net/10495/36319
dc.identifier.eissn.none.fl_str_mv 2382-4581
dc.identifier.url.spa.fl_str_mv http://www.scielo.org.co/pdf/ctyf/v5n4/v5n4a03.pdf
identifier_str_mv Calderón, J. A., Bonilla, G. F. & Carreño, J. A. (2014). The corrosion process of P-110 steel in stimulation fluids used in the oil industry. CT&F - Ciencia, Tecnología y Futuro, 5(4), 35-48
0122-5383
2382-4581
url https://hdl.handle.net/10495/36319
http://www.scielo.org.co/pdf/ctyf/v5n4/v5n4a03.pdf
dc.language.iso.spa.fl_str_mv eng
language eng
dc.relation.ispartofjournalabbrev.spa.fl_str_mv CT&F
dc.relation.citationendpage.spa.fl_str_mv 47
dc.relation.citationissue.spa.fl_str_mv 4
dc.relation.citationstartpage.spa.fl_str_mv 35
dc.relation.citationvolume.spa.fl_str_mv 5
dc.relation.ispartofjournal.spa.fl_str_mv CT y F - Ciencia, Tecnologia y Futuro
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institution Universidad de Antioquia
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spelling Calderón Gutiérrez, Jorge AndrésBonilla Muñetones, Gloria FernandaCarreño, Javier AlejandroCentro de Investigación Innovación y Desarrollo de Materiales (CIDEMAT)2023-08-22T20:29:39Z2023-08-22T20:29:39Z2014Calderón, J. A., Bonilla, G. F. & Carreño, J. A. (2014). The corrosion process of P-110 steel in stimulation fluids used in the oil industry. CT&F - Ciencia, Tecnología y Futuro, 5(4), 35-480122-5383https://hdl.handle.net/10495/363192382-4581http://www.scielo.org.co/pdf/ctyf/v5n4/v5n4a03.pdfABSTRACT: The use of chelating agents in the oil well stimulation processes has been proposed as an alternative to the acid treatment when the formations damage do not allow the usage of strong chemical attack. However, this procedure can arouse the corrosion of the steel used in the infrastructure of the oil production. In this study, the corrosion kinetics of the P-110 steel in ethylenediaminetetraacetic acid (EDTA) based fluids is assessed under different conditions of evaluation. Linear polarization was performed in different hydrodynamic regimes and at different temperatures, in order to evaluate the kinetic of steel corrosion. The working electrolyte solution comprises 10% disodium EDTA and 20% tetrasodium EDTA. The increase of temperature from 25 to 80°C in both electrolytes increments the corrosion rate of steel in at least one order of magnitude; particularly in EDTA-Na2 solutions. Corrosion rates of 0.29x101 and 1.67x102 mm·y-1 were measured at 25 and 80°C, respectively. The hydrodynamic regime plays an important role in the corrosion of steel only in the disodium solution, where corrosion rates were increased at higher rotation speeds of the electrode. The cathodic depolarization effect is more important in the EDTA-Na2 than in the EDTA-Na4 solution, making it more corrosive.RESUMEN: El uso de agentes quelantes en procesos de estimulación de pozos de petróleo ha sido propuesto como alternativa al tratamiento ácido cuando el daño de formaciones no permite un ataque químico fuerte. Sin embargo, este procedimiento puede incentivar la corrosión del acero utilizado en la infraestructura de producción de petróleo. En este estudio se evaluó la cinética de corrosión del acero P-110 en fluidos base ácido etildiaminotetraacético (EDTA) en diferentes condiciones. Medidas de polarización lineal fueron realizadas en diferentes regímenes hidrodinámicos y a diferentes temperaturas para evaluar la cinética de corrosión del acero. El electrolito de trabajo consistió en soluciones de EDTA disódico al 10%, y EDTA tetrasódico al 20%. El incremento de la temperatura de 25 a 80°C en ambos electrolitos aumenta la tasa de corrosión del acero en un orden de magnitud, particularmente en soluciones de EDTA-Na2. Las velocidades de corrosión fueron de 0.29x101 y 1.67x102 mm·y-1 a 25 y 80°C, respectivamente. El régimen hidrodinámico juega un papel importante solo en la solución disódica, en la cual las velocidades de corrosión se incrementaron a altas velocidades de rotación del electrodo. El efecto de despolarización catódica en la solución de EDTA-Na2 es más importante que en la solución de EDTA-Na4, haciéndola más corrosiva.RESUMO: Ouso de agentes quelantes em processos de estimulação de poços de petróleo foi proposto como alternativa ao tratamento ácido quando o dano de formações não permite um ataque químico forte. Porém, este procedimento pode incentivar a corrosão do aço utilizado na infraestrutura da produção de petróleo. Neste estudo avaliou-se a cinética de corrosão do aço P-110 em fluídos base ácido etilenodiamino tetra-acético (EDTA) em diferentes condições. Medidas de polarização linear foram realizadas em diferentes regimes hidrodinâmicos e a diferentes temperaturas para avaliar a cinética de corrosão do aço. O eletrólito de trabalho consistiu em soluções de EDTA dissódico a 10%, e EDTA tetrassódico a 20%. O aumento da temperatura de 25 a 80°C em ambos os eletrólitos aumenta a taxa de corrosão do aço em uma ordem de magnitude, particularmente em soluções de EDTA-Na2. As velocidades de corrosão foram de 0.29x101 e 1.67x102 mm.y-1 a 25 e 80°C, respectivamente. O regime hidrodinâmico joga um papel importante só na solução dissódica, na qual as velocidades de corrosão aumentaram a altas velocidades de rotação do eletrodo. O efeito de despolarização catódica na solução de EDTA-Na2 é mais importante que na solução de EDTA-Na4, fazendo-a mais corrosivaMinisterio de Ciencia, Tecnología e InnovaciónUniversidad de Antioquia. Vicerrectoría de investigación. Comité para el Desarrollo de la Investigación - CODICOL000792713application/pdfengEditorial Board CT&FPiedecuesta, Colombiahttp://creativecommons.org/licenses/by-nc-sa/2.5/co/https://creativecommons.org/licenses/by-nc-sa/4.0/info:eu-repo/semantics/openAccesshttp://purl.org/coar/access_right/c_abf2The corrosion process of p-110 steel in stimulation fluids used in the oil industryEl proceso de corrosión del acero p-110 en fluidos de estimulación utilizados en la industria del petróleoArtículo de investigaciónhttp://purl.org/coar/resource_type/c_2df8fbb1https://purl.org/redcol/resource_type/ARThttp://purl.org/coar/version/c_970fb48d4fbd8a85info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionÁcido EdéticoEdetic AcidRecursos petrolerosPetroleum resourcesCorrosiónCorrosionElectrochemical techniquesMetal dissolutionhttp://vocabularies.unesco.org/thesaurus/concept14587http://vocabularies.unesco.org/thesaurus/concept5010CT&F474355CT y F - Ciencia, Tecnologia y Futuro0381-2013 Diáspora 2011N° MDC10-1-03RoR: 048jthh02RoR: 03bp5hc83PublicationORIGINALCalderonJorge_2014_CorrosionProcess.pdfCalderonJorge_2014_CorrosionProcess.pdfArtículo de investigaciónapplication/pdf1436896https://bibliotecadigital.udea.edu.co/bitstreams/50a2e505-dfed-45a6-a0c3-a90747ba535a/download6dc8fb446550b86c4a7a3f66c857d978MD51trueAnonymousREADCC-LICENSElicense_rdflicense_rdfapplication/rdf+xml; charset=utf-81051https://bibliotecadigital.udea.edu.co/bitstreams/6855028d-a3b6-42d7-a744-828400ce1aae/downloade2060682c9c70d4d30c83c51448f4eedMD52falseAnonymousREADLICENSElicense.txtlicense.txttext/plain; charset=utf-81748https://bibliotecadigital.udea.edu.co/bitstreams/a43a0289-9bb7-4a01-a995-a78ac0fa49bf/download8a4605be74aa9ea9d79846c1fba20a33MD53falseAnonymousREADTEXTCalderonJorge_2014_CorrosionProcess.pdf.txtCalderonJorge_2014_CorrosionProcess.pdf.txtExtracted texttext/plain39695https://bibliotecadigital.udea.edu.co/bitstreams/ced716bc-3c36-4462-88b8-519563d991c5/downloada8fd9a4a9cb23c89a72f98bb6a4f6850MD54falseAnonymousREADTHUMBNAILCalderonJorge_2014_CorrosionProcess.pdf.jpgCalderonJorge_2014_CorrosionProcess.pdf.jpgGenerated Thumbnailimage/jpeg10736https://bibliotecadigital.udea.edu.co/bitstreams/edce122e-1264-4658-8800-e4dfdbc7c201/download602d1fa70f9576c9b0a1b870485775d4MD55falseAnonymousREAD10495/36319oai:bibliotecadigital.udea.edu.co:10495/363192025-03-26 21:56:30.713http://creativecommons.org/licenses/by-nc-sa/2.5/co/open.accesshttps://bibliotecadigital.udea.edu.coRepositorio Institucional de la Universidad de Antioquiaaplicacionbibliotecadigitalbiblioteca@udea.edu.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