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pH prediction in concentrated aqueous solutions under high pressure of acid gases and high temperature
•An extended model for pH prediction in oil and gas environments under high pressure and high temperature is proposed.•The model takes into account gas fugacities calculated using Soreide and Whitson model.•The activity of components in the liquid phase is calculated with Pitzer’s model.•The model s...
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Published in: | Corrosion science 2013-08, Vol.73, p.143-149 |
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Main Authors: | , , , , , , , |
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container_end_page | 149 |
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container_start_page | 143 |
container_title | Corrosion science |
container_volume | 73 |
creator | Plennevaux, C. Ferrando, N. Kittel, J. Frégonèse, M. Normand, B. Cassagne, T. Ropital, F. Bonis, M. |
description | •An extended model for pH prediction in oil and gas environments under high pressure and high temperature is proposed.•The model takes into account gas fugacities calculated using Soreide and Whitson model.•The activity of components in the liquid phase is calculated with Pitzer’s model.•The model shows a good agreement with experimental data.
An extended model for pH prediction in oil and gas environments has been developed. Accurate pH calculations for high pressure and high temperature applications depends mainly on CO2 and H2S partial pressures, the ionic strength, the chemical composition of the solution, and the temperature. Accounting for the non-ideal behaviors of liquid and gas phases allows pH calculations up to 200°C, 2000bar total pressure, and ionic strengths up to 5molL−1. The results are consistent with experimental measurements and with other models reported in the literature. |
doi_str_mv | 10.1016/j.corsci.2013.04.002 |
format | article |
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An extended model for pH prediction in oil and gas environments has been developed. Accurate pH calculations for high pressure and high temperature applications depends mainly on CO2 and H2S partial pressures, the ionic strength, the chemical composition of the solution, and the temperature. Accounting for the non-ideal behaviors of liquid and gas phases allows pH calculations up to 200°C, 2000bar total pressure, and ionic strengths up to 5molL−1. The results are consistent with experimental measurements and with other models reported in the literature.</description><identifier>ISSN: 0010-938X</identifier><identifier>EISSN: 1879-0496</identifier><identifier>DOI: 10.1016/j.corsci.2013.04.002</identifier><identifier>CODEN: CRRSAA</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>A. Acid solutions ; Accounting ; Applied sciences ; B. Modeling studies ; C. Thermodynamic diagrams ; Carbon dioxide ; Chemical Sciences ; Corrosion ; Corrosion environments ; Exact sciences and technology ; Gas phases ; Liquids ; Mathematical models ; Metals. Metallurgy ; Natural gas ; Strength</subject><ispartof>Corrosion science, 2013-08, Vol.73, p.143-149</ispartof><rights>2013 Elsevier Ltd</rights><rights>2014 INIST-CNRS</rights><rights>Distributed under a Creative Commons Attribution 4.0 International License</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c449t-b63ea30931ca641148030039ce8bb2bb60515952c39f0c6b1e144f631732f7933</citedby><cites>FETCH-LOGICAL-c449t-b63ea30931ca641148030039ce8bb2bb60515952c39f0c6b1e144f631732f7933</cites><orcidid>0000-0002-8023-1153</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>230,314,780,784,885,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=27448963$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://ifp.hal.science/hal-02420555$$DView record in HAL$$Hfree_for_read</backlink></links><search><creatorcontrib>Plennevaux, C.</creatorcontrib><creatorcontrib>Ferrando, N.</creatorcontrib><creatorcontrib>Kittel, J.</creatorcontrib><creatorcontrib>Frégonèse, M.</creatorcontrib><creatorcontrib>Normand, B.</creatorcontrib><creatorcontrib>Cassagne, T.</creatorcontrib><creatorcontrib>Ropital, F.</creatorcontrib><creatorcontrib>Bonis, M.</creatorcontrib><title>pH prediction in concentrated aqueous solutions under high pressure of acid gases and high temperature</title><title>Corrosion science</title><description>•An extended model for pH prediction in oil and gas environments under high pressure and high temperature is proposed.•The model takes into account gas fugacities calculated using Soreide and Whitson model.•The activity of components in the liquid phase is calculated with Pitzer’s model.•The model shows a good agreement with experimental data.
An extended model for pH prediction in oil and gas environments has been developed. Accurate pH calculations for high pressure and high temperature applications depends mainly on CO2 and H2S partial pressures, the ionic strength, the chemical composition of the solution, and the temperature. Accounting for the non-ideal behaviors of liquid and gas phases allows pH calculations up to 200°C, 2000bar total pressure, and ionic strengths up to 5molL−1. The results are consistent with experimental measurements and with other models reported in the literature.</description><subject>A. Acid solutions</subject><subject>Accounting</subject><subject>Applied sciences</subject><subject>B. Modeling studies</subject><subject>C. Thermodynamic diagrams</subject><subject>Carbon dioxide</subject><subject>Chemical Sciences</subject><subject>Corrosion</subject><subject>Corrosion environments</subject><subject>Exact sciences and technology</subject><subject>Gas phases</subject><subject>Liquids</subject><subject>Mathematical models</subject><subject>Metals. 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Acid solutions</topic><topic>Accounting</topic><topic>Applied sciences</topic><topic>B. Modeling studies</topic><topic>C. Thermodynamic diagrams</topic><topic>Carbon dioxide</topic><topic>Chemical Sciences</topic><topic>Corrosion</topic><topic>Corrosion environments</topic><topic>Exact sciences and technology</topic><topic>Gas phases</topic><topic>Liquids</topic><topic>Mathematical models</topic><topic>Metals. Metallurgy</topic><topic>Natural gas</topic><topic>Strength</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Plennevaux, C.</creatorcontrib><creatorcontrib>Ferrando, N.</creatorcontrib><creatorcontrib>Kittel, J.</creatorcontrib><creatorcontrib>Frégonèse, M.</creatorcontrib><creatorcontrib>Normand, B.</creatorcontrib><creatorcontrib>Cassagne, T.</creatorcontrib><creatorcontrib>Ropital, F.</creatorcontrib><creatorcontrib>Bonis, M.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Corrosion Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><collection>Hyper Article en Ligne (HAL)</collection><collection>Hyper Article en Ligne (HAL) (Open Access)</collection><jtitle>Corrosion science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Plennevaux, C.</au><au>Ferrando, N.</au><au>Kittel, J.</au><au>Frégonèse, M.</au><au>Normand, B.</au><au>Cassagne, T.</au><au>Ropital, F.</au><au>Bonis, M.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>pH prediction in concentrated aqueous solutions under high pressure of acid gases and high temperature</atitle><jtitle>Corrosion science</jtitle><date>2013-08-01</date><risdate>2013</risdate><volume>73</volume><spage>143</spage><epage>149</epage><pages>143-149</pages><issn>0010-938X</issn><eissn>1879-0496</eissn><coden>CRRSAA</coden><abstract>•An extended model for pH prediction in oil and gas environments under high pressure and high temperature is proposed.•The model takes into account gas fugacities calculated using Soreide and Whitson model.•The activity of components in the liquid phase is calculated with Pitzer’s model.•The model shows a good agreement with experimental data.
An extended model for pH prediction in oil and gas environments has been developed. Accurate pH calculations for high pressure and high temperature applications depends mainly on CO2 and H2S partial pressures, the ionic strength, the chemical composition of the solution, and the temperature. Accounting for the non-ideal behaviors of liquid and gas phases allows pH calculations up to 200°C, 2000bar total pressure, and ionic strengths up to 5molL−1. The results are consistent with experimental measurements and with other models reported in the literature.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.corsci.2013.04.002</doi><tpages>7</tpages><orcidid>https://orcid.org/0000-0002-8023-1153</orcidid><oa>free_for_read</oa></addata></record> |
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subjects | A. Acid solutions Accounting Applied sciences B. Modeling studies C. Thermodynamic diagrams Carbon dioxide Chemical Sciences Corrosion Corrosion environments Exact sciences and technology Gas phases Liquids Mathematical models Metals. Metallurgy Natural gas Strength |
title | pH prediction in concentrated aqueous solutions under high pressure of acid gases and high temperature |
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