High temperature electrochemical reaction parameters affecting elecrochemical corrosion potential of type 316L stainless steel
High temperature electrochemical reaction parameters for type 316 L stainless steel (316 L SS) have been determined based on data measured in pure water at high temperatures to realize an analytical model that can predict electrochemical corrosion potential (ECP) of 316 L SS without using any adjust...
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| Veröffentlicht in: | Journal of nuclear science and technology 2022-04, Vol.59 (4), p.491-498 |
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| container_end_page | 498 |
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| container_issue | 4 |
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| container_title | Journal of nuclear science and technology |
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| creator | Wada, Yoichi Ishida, Kazushige Tachibana, Masahiko Shimizu, Ryosuke |
| description | High temperature electrochemical reaction parameters for type 316 L stainless steel (316 L SS) have been determined based on data measured in pure water at high temperatures to realize an analytical model that can predict electrochemical corrosion potential (ECP) of 316 L SS without using any adjustment parameters based on ECP data. Behaviors of measured polarization curves for 316 L SS could be explained well with the determined parameters. Calculated ECPs of 316 L SS agreed with measured values in the case that it was acceptable for the model to have an error range of ±0.1 V in a wide oxygen concentration range. However, the error was relatively larger in the range from 10 to 100 ppb oxygen concentration because of the shape of the anodic polarization curve of 316 L SS; in other words, ECP could not be uniquely determined in such an oxygen concentration range. It is expected that the ECP model with the determined electrochemical parameters will have greater validity for, and better interpretability of, the ECPs of SS determined in a boiling water reactor environment. |
| doi_str_mv | 10.1080/00223131.2021.1980447 |
| format | Article |
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Behaviors of measured polarization curves for 316 L SS could be explained well with the determined parameters. Calculated ECPs of 316 L SS agreed with measured values in the case that it was acceptable for the model to have an error range of ±0.1 V in a wide oxygen concentration range. However, the error was relatively larger in the range from 10 to 100 ppb oxygen concentration because of the shape of the anodic polarization curve of 316 L SS; in other words, ECP could not be uniquely determined in such an oxygen concentration range. It is expected that the ECP model with the determined electrochemical parameters will have greater validity for, and better interpretability of, the ECPs of SS determined in a boiling water reactor environment.</description><identifier>ISSN: 0022-3131</identifier><identifier>EISSN: 1881-1248</identifier><identifier>DOI: 10.1080/00223131.2021.1980447</identifier><language>eng</language><publisher>Tokyo: Taylor & Francis</publisher><subject>Anodic polarization ; Austenitic stainless steels ; Boiling water reactors ; BWR ; cathodic reaction ; Corrosion potential ; ECP ; Electrochemical corrosion ; Electrode polarization ; Heat resistant steels ; High temperature ; Mathematical models ; Oxygen ; Parameters ; polarization curve ; Stainless steel</subject><ispartof>Journal of nuclear science and technology, 2022-04, Vol.59 (4), p.491-498</ispartof><rights>2021 Atomic Energy Society of Japan. All rights reserved. 2021</rights><rights>2021 Atomic Energy Society of Japan. 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Behaviors of measured polarization curves for 316 L SS could be explained well with the determined parameters. Calculated ECPs of 316 L SS agreed with measured values in the case that it was acceptable for the model to have an error range of ±0.1 V in a wide oxygen concentration range. However, the error was relatively larger in the range from 10 to 100 ppb oxygen concentration because of the shape of the anodic polarization curve of 316 L SS; in other words, ECP could not be uniquely determined in such an oxygen concentration range. It is expected that the ECP model with the determined electrochemical parameters will have greater validity for, and better interpretability of, the ECPs of SS determined in a boiling water reactor environment.</description><subject>Anodic polarization</subject><subject>Austenitic stainless steels</subject><subject>Boiling water reactors</subject><subject>BWR</subject><subject>cathodic reaction</subject><subject>Corrosion potential</subject><subject>ECP</subject><subject>Electrochemical corrosion</subject><subject>Electrode polarization</subject><subject>Heat resistant steels</subject><subject>High temperature</subject><subject>Mathematical models</subject><subject>Oxygen</subject><subject>Parameters</subject><subject>polarization curve</subject><subject>Stainless steel</subject><issn>0022-3131</issn><issn>1881-1248</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2022</creationdate><recordtype>article</recordtype><recordid>eNp90E1LAzEQBuAgCtaPnyAseN6aSbbZ9KaIWqHgRc8hphON7G7WSYr04m83tQqePOWDZ2aYl7Ez4FPgml9wLoQECVPBBUxhrnnTtHtsAlpDDaLR-2yyNfUWHbKjlN7KUzVKT9jnIry8Vhn7EcnmNWGFHbpM0b1iH5ztKkLrcohDNVqyPWakVFnvCwrDy7f-g10kiulbx4xDDuUv-ipvRqwkqGWVsg1DhymVG2J3wg687RKe_pzH7On25vF6US8f7u6vr5a1k1Ln2q30s3XzFcwVcOvksxUOxAwa3padOLTOSyEQRatmjeZeF-KAOydV4-fCyWN2vus7UnxfY8rmLa5pKCONUHLWNkpqVdRsp8pKKRF6M1LoLW0McLON2vxGbbZRm5-oS93lri4MPlJvPyJ1K5PtpovkyQ4uJCP_b_EF9wuHWQ</recordid><startdate>20220403</startdate><enddate>20220403</enddate><creator>Wada, Yoichi</creator><creator>Ishida, Kazushige</creator><creator>Tachibana, Masahiko</creator><creator>Shimizu, Ryosuke</creator><general>Taylor & Francis</general><general>Taylor & Francis Ltd</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20220403</creationdate><title>High temperature electrochemical reaction parameters affecting elecrochemical corrosion potential of type 316L stainless steel</title><author>Wada, Yoichi ; Ishida, Kazushige ; Tachibana, Masahiko ; Shimizu, Ryosuke</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c338t-cd8bac9d19610ac3ba2c1251407313017cf322ee2765480f8c3bc10cc364f92c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2022</creationdate><topic>Anodic polarization</topic><topic>Austenitic stainless steels</topic><topic>Boiling water reactors</topic><topic>BWR</topic><topic>cathodic reaction</topic><topic>Corrosion potential</topic><topic>ECP</topic><topic>Electrochemical corrosion</topic><topic>Electrode polarization</topic><topic>Heat resistant steels</topic><topic>High temperature</topic><topic>Mathematical models</topic><topic>Oxygen</topic><topic>Parameters</topic><topic>polarization curve</topic><topic>Stainless steel</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Wada, Yoichi</creatorcontrib><creatorcontrib>Ishida, Kazushige</creatorcontrib><creatorcontrib>Tachibana, Masahiko</creatorcontrib><creatorcontrib>Shimizu, Ryosuke</creatorcontrib><collection>CrossRef</collection><jtitle>Journal of nuclear science and technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Wada, Yoichi</au><au>Ishida, Kazushige</au><au>Tachibana, Masahiko</au><au>Shimizu, Ryosuke</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>High temperature electrochemical reaction parameters affecting elecrochemical corrosion potential of type 316L stainless steel</atitle><jtitle>Journal of nuclear science and technology</jtitle><date>2022-04-03</date><risdate>2022</risdate><volume>59</volume><issue>4</issue><spage>491</spage><epage>498</epage><pages>491-498</pages><issn>0022-3131</issn><eissn>1881-1248</eissn><abstract>High temperature electrochemical reaction parameters for type 316 L stainless steel (316 L SS) have been determined based on data measured in pure water at high temperatures to realize an analytical model that can predict electrochemical corrosion potential (ECP) of 316 L SS without using any adjustment parameters based on ECP data. Behaviors of measured polarization curves for 316 L SS could be explained well with the determined parameters. Calculated ECPs of 316 L SS agreed with measured values in the case that it was acceptable for the model to have an error range of ±0.1 V in a wide oxygen concentration range. However, the error was relatively larger in the range from 10 to 100 ppb oxygen concentration because of the shape of the anodic polarization curve of 316 L SS; in other words, ECP could not be uniquely determined in such an oxygen concentration range. It is expected that the ECP model with the determined electrochemical parameters will have greater validity for, and better interpretability of, the ECPs of SS determined in a boiling water reactor environment.</abstract><cop>Tokyo</cop><pub>Taylor & Francis</pub><doi>10.1080/00223131.2021.1980447</doi><tpages>8</tpages></addata></record> |
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| ispartof | Journal of nuclear science and technology, 2022-04, Vol.59 (4), p.491-498 |
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| language | eng |
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| source | Alma/SFX Local Collection |
| subjects | Anodic polarization Austenitic stainless steels Boiling water reactors BWR cathodic reaction Corrosion potential ECP Electrochemical corrosion Electrode polarization Heat resistant steels High temperature Mathematical models Oxygen Parameters polarization curve Stainless steel |
| title | High temperature electrochemical reaction parameters affecting elecrochemical corrosion potential of type 316L stainless steel |
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