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Novel Synergistic Process of Impurities Extraction and Phophogypsum Crystallization Control in Wet-Process Phosphoric Acid

[Image: see text] Phosphogypsum, as a byproduct of wet-process phosphoric acid reaction, has caused many environmental pollution problems. To improve the property and purity of phosphogypsum in the wet-process phosphoric acid process, a liquid–solid–liquid three-phase acid hydrolysis synergistic ext...

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Autores principales: Zhu, Ganyu, Yang, Yunrui, He, Lei, Li, Huiquan, Meng, Ziheng, Zheng, Guangming, Li, Fang, Su, Xiaodan, Xi, Benjun, Li, Zhongjun
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2023
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10413463/
https://www.ncbi.nlm.nih.gov/pubmed/37576616
http://dx.doi.org/10.1021/acsomega.3c01168
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author Zhu, Ganyu
Yang, Yunrui
He, Lei
Li, Huiquan
Meng, Ziheng
Zheng, Guangming
Li, Fang
Su, Xiaodan
Xi, Benjun
Li, Zhongjun
author_facet Zhu, Ganyu
Yang, Yunrui
He, Lei
Li, Huiquan
Meng, Ziheng
Zheng, Guangming
Li, Fang
Su, Xiaodan
Xi, Benjun
Li, Zhongjun
author_sort Zhu, Ganyu
collection PubMed
description [Image: see text] Phosphogypsum, as a byproduct of wet-process phosphoric acid reaction, has caused many environmental pollution problems. To improve the property and purity of phosphogypsum in the wet-process phosphoric acid process, a liquid–solid–liquid three-phase acid hydrolysis synergistic extraction reaction system was established by adding a certain amount of extractant in the actual production process. In order to study the extraction effect and residue of impurities in the reaction system, the phase, morphology, and impurity occurrences of phosphogypsum were systematically analyzed. The results showed that when the reaction time was 7 h, the reaction temperature was 80 °C, the reaction speed was 200 r/min, the volume ratio of the extractant to diluent (dilution ratio) was 1:4 and the volume ratio of the oil phase/aqueous phase (O/A ratio) was 1:1, P(2)O(5) conversion was the highest in phosphate rock, and the residual P(2)O(5) content in phosphogypsum was as low as 0.36%. The morphology of the phosphogypsum crystal was uniform and coarse long strip. The main forms of residual impurities were silicate, aluminum fluoride with crystal water, aluminate, phosphate, and fluoride. Meanwhile, the residual amount of main impurities in phosphogypsum was significantly reduced. Through this novel method, the property of phosphogypsum can be improved through the generation process and is greatly beneficial for its utilization and the recycling development of the wet-process phosphoric acid industry.
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spelling pubmed-104134632023-08-11 Novel Synergistic Process of Impurities Extraction and Phophogypsum Crystallization Control in Wet-Process Phosphoric Acid Zhu, Ganyu Yang, Yunrui He, Lei Li, Huiquan Meng, Ziheng Zheng, Guangming Li, Fang Su, Xiaodan Xi, Benjun Li, Zhongjun ACS Omega [Image: see text] Phosphogypsum, as a byproduct of wet-process phosphoric acid reaction, has caused many environmental pollution problems. To improve the property and purity of phosphogypsum in the wet-process phosphoric acid process, a liquid–solid–liquid three-phase acid hydrolysis synergistic extraction reaction system was established by adding a certain amount of extractant in the actual production process. In order to study the extraction effect and residue of impurities in the reaction system, the phase, morphology, and impurity occurrences of phosphogypsum were systematically analyzed. The results showed that when the reaction time was 7 h, the reaction temperature was 80 °C, the reaction speed was 200 r/min, the volume ratio of the extractant to diluent (dilution ratio) was 1:4 and the volume ratio of the oil phase/aqueous phase (O/A ratio) was 1:1, P(2)O(5) conversion was the highest in phosphate rock, and the residual P(2)O(5) content in phosphogypsum was as low as 0.36%. The morphology of the phosphogypsum crystal was uniform and coarse long strip. The main forms of residual impurities were silicate, aluminum fluoride with crystal water, aluminate, phosphate, and fluoride. Meanwhile, the residual amount of main impurities in phosphogypsum was significantly reduced. Through this novel method, the property of phosphogypsum can be improved through the generation process and is greatly beneficial for its utilization and the recycling development of the wet-process phosphoric acid industry. American Chemical Society 2023-07-27 /pmc/articles/PMC10413463/ /pubmed/37576616 http://dx.doi.org/10.1021/acsomega.3c01168 Text en © 2023 The Authors. Published by American Chemical Society https://creativecommons.org/licenses/by-nc-nd/4.0/Permits non-commercial access and re-use, provided that author attribution and integrity are maintained; but does not permit creation of adaptations or other derivative works (https://creativecommons.org/licenses/by-nc-nd/4.0/).
spellingShingle Zhu, Ganyu
Yang, Yunrui
He, Lei
Li, Huiquan
Meng, Ziheng
Zheng, Guangming
Li, Fang
Su, Xiaodan
Xi, Benjun
Li, Zhongjun
Novel Synergistic Process of Impurities Extraction and Phophogypsum Crystallization Control in Wet-Process Phosphoric Acid
title Novel Synergistic Process of Impurities Extraction and Phophogypsum Crystallization Control in Wet-Process Phosphoric Acid
title_full Novel Synergistic Process of Impurities Extraction and Phophogypsum Crystallization Control in Wet-Process Phosphoric Acid
title_fullStr Novel Synergistic Process of Impurities Extraction and Phophogypsum Crystallization Control in Wet-Process Phosphoric Acid
title_full_unstemmed Novel Synergistic Process of Impurities Extraction and Phophogypsum Crystallization Control in Wet-Process Phosphoric Acid
title_short Novel Synergistic Process of Impurities Extraction and Phophogypsum Crystallization Control in Wet-Process Phosphoric Acid
title_sort novel synergistic process of impurities extraction and phophogypsum crystallization control in wet-process phosphoric acid
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10413463/
https://www.ncbi.nlm.nih.gov/pubmed/37576616
http://dx.doi.org/10.1021/acsomega.3c01168
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