Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process
- Autores
- Benitez, Leonel Alberto; Gutierrez, Juan Pablo; Erdmann, Eleonora; Ale Ruiz, Liliana; Tarifa, Enrique Eduardo
- Año de publicación
- 2014
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- Water is probably the most undesirable component found in crude natural gas because its presence can produce hydrate formation, and it can also lead to corrosion or erosion problems in pipes and equipment. Natural gas must be dehydrated before being transported through a long distance to ensure an efficient and trouble-free operation. Thermodynamic modelling of triethyleneglycol (TEG)-water system is still rather inaccurate, especially with regard to systems at high temperature and high TEG concentration. As a consequence, design and operation of absorber towers are affected by the lack of accurate data. Two novel correlations have been developed to estimate the equilibrium water dew point of a natural gas stream by evaluating experimental data and literature. These data were collected and analyzed by means of images scanned with MATLAB software R2012B version. An average percentage error is of 1-2% for linear correlation and it is of 2-3% for non-linear correlation. Results are quite accurate and they are consistent with literature data. Due to the simplicity and precision of the correlations developed in this work, the equations obtained have a great practical value. Consequently, they allow process engineers to perform a quick check of the water dew point at different conditions without using complex expressions or graphics.
Fil: Benitez, Leonel Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones Para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones Para la Industria Química; Argentina
Fil: Gutierrez, Juan Pablo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones Para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones Para la Industria Química; Argentina
Fil: Erdmann, Eleonora. Instituto Tecnológico de Buenos Aires; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones Para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones Para la Industria Química; Argentina
Fil: Ale Ruiz, Liliana. Universidad Nacional de Salta. Consejo de Investigacion; Argentina
Fil: Tarifa, Enrique Eduardo. Universidad Nacional de Jujuy. Facultad de Ingeniería; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas; Argentina - Materia
-
Corrrelation
DewPoint
NaturalGas
TEG
WaterDehydration - 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:11336/22307
Ver los metadatos del registro completo
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Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration processBenitez, Leonel AlbertoGutierrez, Juan PabloErdmann, EleonoraAle Ruiz, LilianaTarifa, Enrique EduardoCorrrelationDewPointNaturalGasTEGWaterDehydrationhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2Water is probably the most undesirable component found in crude natural gas because its presence can produce hydrate formation, and it can also lead to corrosion or erosion problems in pipes and equipment. Natural gas must be dehydrated before being transported through a long distance to ensure an efficient and trouble-free operation. Thermodynamic modelling of triethyleneglycol (TEG)-water system is still rather inaccurate, especially with regard to systems at high temperature and high TEG concentration. As a consequence, design and operation of absorber towers are affected by the lack of accurate data. Two novel correlations have been developed to estimate the equilibrium water dew point of a natural gas stream by evaluating experimental data and literature. These data were collected and analyzed by means of images scanned with MATLAB software R2012B version. An average percentage error is of 1-2% for linear correlation and it is of 2-3% for non-linear correlation. Results are quite accurate and they are consistent with literature data. Due to the simplicity and precision of the correlations developed in this work, the equations obtained have a great practical value. Consequently, they allow process engineers to perform a quick check of the water dew point at different conditions without using complex expressions or graphics.Fil: Benitez, Leonel Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones Para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones Para la Industria Química; ArgentinaFil: Gutierrez, Juan Pablo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones Para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones Para la Industria Química; ArgentinaFil: Erdmann, Eleonora. Instituto Tecnológico de Buenos Aires; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones Para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones Para la Industria Química; ArgentinaFil: Ale Ruiz, Liliana. Universidad Nacional de Salta. Consejo de Investigacion; ArgentinaFil: Tarifa, Enrique Eduardo. Universidad Nacional de Jujuy. Facultad de Ingeniería; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas; ArgentinaIJERA Publication2014-04info: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/11336/22307Benitez, Leonel Alberto; Gutierrez, Juan Pablo; Erdmann, Eleonora; Ale Ruiz, Liliana; Tarifa, Enrique Eduardo; Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process; IJERA Publication; International Journal of Engineering Research and Applications; 4; 4; 4-2014; 114-1192248-9622CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/http://www.ijera.com/papers/Vol4_issue4/Version%201/Q044114119.pdfinfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-10T13:03:02Zoai:ri.conicet.gov.ar:11336/22307instacron: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:34982025-09-10 13:03:03.057CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
dc.title.none.fl_str_mv |
Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process |
title |
Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process |
spellingShingle |
Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process Benitez, Leonel Alberto Corrrelation DewPoint NaturalGas TEG WaterDehydration |
title_short |
Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process |
title_full |
Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process |
title_fullStr |
Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process |
title_full_unstemmed |
Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process |
title_sort |
Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process |
dc.creator.none.fl_str_mv |
Benitez, Leonel Alberto Gutierrez, Juan Pablo Erdmann, Eleonora Ale Ruiz, Liliana Tarifa, Enrique Eduardo |
author |
Benitez, Leonel Alberto |
author_facet |
Benitez, Leonel Alberto Gutierrez, Juan Pablo Erdmann, Eleonora Ale Ruiz, Liliana Tarifa, Enrique Eduardo |
author_role |
author |
author2 |
Gutierrez, Juan Pablo Erdmann, Eleonora Ale Ruiz, Liliana Tarifa, Enrique Eduardo |
author2_role |
author author author author |
dc.subject.none.fl_str_mv |
Corrrelation DewPoint NaturalGas TEG WaterDehydration |
topic |
Corrrelation DewPoint NaturalGas TEG WaterDehydration |
purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
dc.description.none.fl_txt_mv |
Water is probably the most undesirable component found in crude natural gas because its presence can produce hydrate formation, and it can also lead to corrosion or erosion problems in pipes and equipment. Natural gas must be dehydrated before being transported through a long distance to ensure an efficient and trouble-free operation. Thermodynamic modelling of triethyleneglycol (TEG)-water system is still rather inaccurate, especially with regard to systems at high temperature and high TEG concentration. As a consequence, design and operation of absorber towers are affected by the lack of accurate data. Two novel correlations have been developed to estimate the equilibrium water dew point of a natural gas stream by evaluating experimental data and literature. These data were collected and analyzed by means of images scanned with MATLAB software R2012B version. An average percentage error is of 1-2% for linear correlation and it is of 2-3% for non-linear correlation. Results are quite accurate and they are consistent with literature data. Due to the simplicity and precision of the correlations developed in this work, the equations obtained have a great practical value. Consequently, they allow process engineers to perform a quick check of the water dew point at different conditions without using complex expressions or graphics. Fil: Benitez, Leonel Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones Para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones Para la Industria Química; Argentina Fil: Gutierrez, Juan Pablo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones Para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones Para la Industria Química; Argentina Fil: Erdmann, Eleonora. Instituto Tecnológico de Buenos Aires; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones Para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones Para la Industria Química; Argentina Fil: Ale Ruiz, Liliana. Universidad Nacional de Salta. Consejo de Investigacion; Argentina Fil: Tarifa, Enrique Eduardo. Universidad Nacional de Jujuy. Facultad de Ingeniería; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas; Argentina |
description |
Water is probably the most undesirable component found in crude natural gas because its presence can produce hydrate formation, and it can also lead to corrosion or erosion problems in pipes and equipment. Natural gas must be dehydrated before being transported through a long distance to ensure an efficient and trouble-free operation. Thermodynamic modelling of triethyleneglycol (TEG)-water system is still rather inaccurate, especially with regard to systems at high temperature and high TEG concentration. As a consequence, design and operation of absorber towers are affected by the lack of accurate data. Two novel correlations have been developed to estimate the equilibrium water dew point of a natural gas stream by evaluating experimental data and literature. These data were collected and analyzed by means of images scanned with MATLAB software R2012B version. An average percentage error is of 1-2% for linear correlation and it is of 2-3% for non-linear correlation. Results are quite accurate and they are consistent with literature data. Due to the simplicity and precision of the correlations developed in this work, the equations obtained have a great practical value. Consequently, they allow process engineers to perform a quick check of the water dew point at different conditions without using complex expressions or graphics. |
publishDate |
2014 |
dc.date.none.fl_str_mv |
2014-04 |
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/11336/22307 Benitez, Leonel Alberto; Gutierrez, Juan Pablo; Erdmann, Eleonora; Ale Ruiz, Liliana; Tarifa, Enrique Eduardo; Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process; IJERA Publication; International Journal of Engineering Research and Applications; 4; 4; 4-2014; 114-119 2248-9622 CONICET Digital CONICET |
url |
http://hdl.handle.net/11336/22307 |
identifier_str_mv |
Benitez, Leonel Alberto; Gutierrez, Juan Pablo; Erdmann, Eleonora; Ale Ruiz, Liliana; Tarifa, Enrique Eduardo; Two noveland simple correlations to estimate equilibrium water dew point for natural gas dehydration process; IJERA Publication; International Journal of Engineering Research and Applications; 4; 4; 4-2014; 114-119 2248-9622 CONICET Digital CONICET |
dc.language.none.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
info:eu-repo/semantics/altIdentifier/url/http://www.ijera.com/papers/Vol4_issue4/Version%201/Q044114119.pdf |
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 |
IJERA Publication |
publisher.none.fl_str_mv |
IJERA Publication |
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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1842980056835555328 |
score |
12.993085 |