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Investigating the Corrosive Influence of Chloride Ions on Slag Recovery Machine Shells in Power Plants
An effective strategy for achieving cost-effective and environmentally friendly desulfurization wastewater in coal-fired power plants involves the incorporation of desulfurization wastewater into the slag water system. The objective of this study was to analyze the corrosion behavior of Q235-A slag-...
Autores principales: | , , , , , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
MDPI
2023
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10419673/ https://www.ncbi.nlm.nih.gov/pubmed/37569973 http://dx.doi.org/10.3390/ma16155270 |
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author | Yu, Yaohong Bai, Jintao Ma, Xiaohan Wang, Shengxing Hu, Dalong Niu, Jun Zhang, Jiangtao Du, An Sun, Dongqi Lu, Jian Fan, Yongzhe |
author_facet | Yu, Yaohong Bai, Jintao Ma, Xiaohan Wang, Shengxing Hu, Dalong Niu, Jun Zhang, Jiangtao Du, An Sun, Dongqi Lu, Jian Fan, Yongzhe |
author_sort | Yu, Yaohong |
collection | PubMed |
description | An effective strategy for achieving cost-effective and environmentally friendly desulfurization wastewater in coal-fired power plants involves the incorporation of desulfurization wastewater into the slag water system. The objective of this study was to analyze the corrosion behavior of Q235-A slag-picker shell material upon the introduction of FGD wastewater into the slag water system. The dynamic weight loss method, electrochemical testing method and microscopic phase characterization were employed to investigate the impact of varying chloride ion concentrations (ranging from 1000 mg/L to 30,000 mg/L) of flue gas desulfurization wastewater (FGD wastewater) on the corrosion of Q235-A slag-picker shell material. The test results indicate that as the concentration of chloride ions increases, the corrosion rate increases from 1.1487 mm/a to 1.5590 mm/a when the concentration is less than 10,000 mg/L. However, when the concentration exceeds 10,000 mg/L, the corrosion rate decreases from 1.559 mm/a to 1.0393 mm/a. The corrosion rate is above 1 mm/a at all concentrations. As the Cl(−) concentration, the quality of the corrosion product film initially increases and then decreases. The primary components of the corrosion product are α- FeOOH, γ-FeOOH, β-FeOOH, Fe(3)O(4) and γ-Fe(2)O(3). |
format | Online Article Text |
id | pubmed-10419673 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2023 |
publisher | MDPI |
record_format | MEDLINE/PubMed |
spelling | pubmed-104196732023-08-12 Investigating the Corrosive Influence of Chloride Ions on Slag Recovery Machine Shells in Power Plants Yu, Yaohong Bai, Jintao Ma, Xiaohan Wang, Shengxing Hu, Dalong Niu, Jun Zhang, Jiangtao Du, An Sun, Dongqi Lu, Jian Fan, Yongzhe Materials (Basel) Article An effective strategy for achieving cost-effective and environmentally friendly desulfurization wastewater in coal-fired power plants involves the incorporation of desulfurization wastewater into the slag water system. The objective of this study was to analyze the corrosion behavior of Q235-A slag-picker shell material upon the introduction of FGD wastewater into the slag water system. The dynamic weight loss method, electrochemical testing method and microscopic phase characterization were employed to investigate the impact of varying chloride ion concentrations (ranging from 1000 mg/L to 30,000 mg/L) of flue gas desulfurization wastewater (FGD wastewater) on the corrosion of Q235-A slag-picker shell material. The test results indicate that as the concentration of chloride ions increases, the corrosion rate increases from 1.1487 mm/a to 1.5590 mm/a when the concentration is less than 10,000 mg/L. However, when the concentration exceeds 10,000 mg/L, the corrosion rate decreases from 1.559 mm/a to 1.0393 mm/a. The corrosion rate is above 1 mm/a at all concentrations. As the Cl(−) concentration, the quality of the corrosion product film initially increases and then decreases. The primary components of the corrosion product are α- FeOOH, γ-FeOOH, β-FeOOH, Fe(3)O(4) and γ-Fe(2)O(3). MDPI 2023-07-27 /pmc/articles/PMC10419673/ /pubmed/37569973 http://dx.doi.org/10.3390/ma16155270 Text en © 2023 by the authors. https://creativecommons.org/licenses/by/4.0/Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/). |
spellingShingle | Article Yu, Yaohong Bai, Jintao Ma, Xiaohan Wang, Shengxing Hu, Dalong Niu, Jun Zhang, Jiangtao Du, An Sun, Dongqi Lu, Jian Fan, Yongzhe Investigating the Corrosive Influence of Chloride Ions on Slag Recovery Machine Shells in Power Plants |
title | Investigating the Corrosive Influence of Chloride Ions on Slag Recovery Machine Shells in Power Plants |
title_full | Investigating the Corrosive Influence of Chloride Ions on Slag Recovery Machine Shells in Power Plants |
title_fullStr | Investigating the Corrosive Influence of Chloride Ions on Slag Recovery Machine Shells in Power Plants |
title_full_unstemmed | Investigating the Corrosive Influence of Chloride Ions on Slag Recovery Machine Shells in Power Plants |
title_short | Investigating the Corrosive Influence of Chloride Ions on Slag Recovery Machine Shells in Power Plants |
title_sort | investigating the corrosive influence of chloride ions on slag recovery machine shells in power plants |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10419673/ https://www.ncbi.nlm.nih.gov/pubmed/37569973 http://dx.doi.org/10.3390/ma16155270 |
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