Zhenning Liu , Zhenan Jin , Linlin Tong , Jiangping Huang , Tenghao Yang
{"title":"利用 NH2SO3H 焙烧工艺从磷酸铁锂电池废液中提取金属的非等温动力学研究","authors":"Zhenning Liu , Zhenan Jin , Linlin Tong , Jiangping Huang , Tenghao Yang","doi":"10.1016/j.psep.2024.11.043","DOIUrl":null,"url":null,"abstract":"<div><div>The non-isothermal kinetics of retired lithium iron phosphate (LiFePO<sub>4</sub>) battery powder and amino sulfonic acid (NH<sub>2</sub>SO<sub>3</sub>H) roasting were studied using TG-DSC. The results show that there are three stages of weight loss: loss of adsorbed water, decomposition and reaction of NH<sub>2</sub>SO<sub>3</sub>H (stage Ⅱ), and formation and growth of Li and Fe sulfate nuclei (stage Ⅲ). The apparent activation energy (E) and pre-exponential factor (ln(A)) of NH<sub>2</sub>SO<sub>3</sub>H decomposition and reaction were 159.85 kJ/mol and 32.02 S<sup>−1</sup>, respectively. Similarly, the apparent E and ln(A) formed by Li and Fe sulfate were 113.89 kJ/mol and 11.55 S<sup>−1</sup>, respectively. Furthermore, the formation of new phases in the second stage reaction is controlled by nucleation and growth. The nucleation and growth of Li and Fe sulfates in the third stage not only occur at this stage, but their rates are also controlled by diffusion. The dynamic equations for the second and third stages are as follows:</div><div><span><math><mrow><mo>[</mo><msup><mrow><mo>−</mo><mi>ln</mi><mo>(</mo><mn>1</mn><mo>−</mo><mi>α</mi><mo>)</mo><mo>]</mo></mrow><mrow><mfrac><mrow><mn>1</mn></mrow><mrow><mn>3</mn></mrow></mfrac></mrow></msup></mrow></math></span>=8.06<span><math><mrow><mo>×</mo><msup><mrow><mn>10</mn></mrow><mrow><mn>13</mn></mrow></msup></mrow></math></span>exp(-<span><math><mfrac><mrow><mn>1.60</mn><mo>×</mo><msup><mrow><mn>10</mn></mrow><mrow><mn>5</mn></mrow></msup></mrow><mrow><mi>RT</mi></mrow></mfrac></math></span>)t</div><div><span><math><mrow><mo>[</mo><msup><mrow><mo>−</mo><mi>ln</mi><mo>(</mo><mn>1</mn><mo>−</mo><mi>α</mi><mo>)</mo><mo>]</mo></mrow><mrow><mfrac><mrow><mn>2</mn></mrow><mrow><mn>3</mn></mrow></mfrac></mrow></msup></mrow></math></span>=1.04<span><math><mrow><mo>×</mo><msup><mrow><mn>10</mn></mrow><mrow><mn>5</mn></mrow></msup></mrow></math></span>exp(-<span><math><mfrac><mrow><mn>1.14</mn><mo>×</mo><msup><mrow><mn>10</mn></mrow><mrow><mn>5</mn></mrow></msup></mrow><mrow><mi>RT</mi></mrow></mfrac></math></span>)t</div></div>","PeriodicalId":20743,"journal":{"name":"Process Safety and Environmental Protection","volume":"193 ","pages":"Pages 87-94"},"PeriodicalIF":6.9000,"publicationDate":"2024-11-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"A non-isothermal kinetic study on the extraction of metals from spent lithium iron phosphate batteries using the NH2SO3H roasting process\",\"authors\":\"Zhenning Liu , Zhenan Jin , Linlin Tong , Jiangping Huang , Tenghao Yang\",\"doi\":\"10.1016/j.psep.2024.11.043\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>The non-isothermal kinetics of retired lithium iron phosphate (LiFePO<sub>4</sub>) battery powder and amino sulfonic acid (NH<sub>2</sub>SO<sub>3</sub>H) roasting were studied using TG-DSC. The results show that there are three stages of weight loss: loss of adsorbed water, decomposition and reaction of NH<sub>2</sub>SO<sub>3</sub>H (stage Ⅱ), and formation and growth of Li and Fe sulfate nuclei (stage Ⅲ). The apparent activation energy (E) and pre-exponential factor (ln(A)) of NH<sub>2</sub>SO<sub>3</sub>H decomposition and reaction were 159.85 kJ/mol and 32.02 S<sup>−1</sup>, respectively. Similarly, the apparent E and ln(A) formed by Li and Fe sulfate were 113.89 kJ/mol and 11.55 S<sup>−1</sup>, respectively. Furthermore, the formation of new phases in the second stage reaction is controlled by nucleation and growth. The nucleation and growth of Li and Fe sulfates in the third stage not only occur at this stage, but their rates are also controlled by diffusion. The dynamic equations for the second and third stages are as follows:</div><div><span><math><mrow><mo>[</mo><msup><mrow><mo>−</mo><mi>ln</mi><mo>(</mo><mn>1</mn><mo>−</mo><mi>α</mi><mo>)</mo><mo>]</mo></mrow><mrow><mfrac><mrow><mn>1</mn></mrow><mrow><mn>3</mn></mrow></mfrac></mrow></msup></mrow></math></span>=8.06<span><math><mrow><mo>×</mo><msup><mrow><mn>10</mn></mrow><mrow><mn>13</mn></mrow></msup></mrow></math></span>exp(-<span><math><mfrac><mrow><mn>1.60</mn><mo>×</mo><msup><mrow><mn>10</mn></mrow><mrow><mn>5</mn></mrow></msup></mrow><mrow><mi>RT</mi></mrow></mfrac></math></span>)t</div><div><span><math><mrow><mo>[</mo><msup><mrow><mo>−</mo><mi>ln</mi><mo>(</mo><mn>1</mn><mo>−</mo><mi>α</mi><mo>)</mo><mo>]</mo></mrow><mrow><mfrac><mrow><mn>2</mn></mrow><mrow><mn>3</mn></mrow></mfrac></mrow></msup></mrow></math></span>=1.04<span><math><mrow><mo>×</mo><msup><mrow><mn>10</mn></mrow><mrow><mn>5</mn></mrow></msup></mrow></math></span>exp(-<span><math><mfrac><mrow><mn>1.14</mn><mo>×</mo><msup><mrow><mn>10</mn></mrow><mrow><mn>5</mn></mrow></msup></mrow><mrow><mi>RT</mi></mrow></mfrac></math></span>)t</div></div>\",\"PeriodicalId\":20743,\"journal\":{\"name\":\"Process Safety and Environmental Protection\",\"volume\":\"193 \",\"pages\":\"Pages 87-94\"},\"PeriodicalIF\":6.9000,\"publicationDate\":\"2024-11-10\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Process Safety and Environmental Protection\",\"FirstCategoryId\":\"93\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0957582024014563\",\"RegionNum\":2,\"RegionCategory\":\"环境科学与生态学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Process Safety and Environmental Protection","FirstCategoryId":"93","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0957582024014563","RegionNum":2,"RegionCategory":"环境科学与生态学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
A non-isothermal kinetic study on the extraction of metals from spent lithium iron phosphate batteries using the NH2SO3H roasting process
The non-isothermal kinetics of retired lithium iron phosphate (LiFePO4) battery powder and amino sulfonic acid (NH2SO3H) roasting were studied using TG-DSC. The results show that there are three stages of weight loss: loss of adsorbed water, decomposition and reaction of NH2SO3H (stage Ⅱ), and formation and growth of Li and Fe sulfate nuclei (stage Ⅲ). The apparent activation energy (E) and pre-exponential factor (ln(A)) of NH2SO3H decomposition and reaction were 159.85 kJ/mol and 32.02 S−1, respectively. Similarly, the apparent E and ln(A) formed by Li and Fe sulfate were 113.89 kJ/mol and 11.55 S−1, respectively. Furthermore, the formation of new phases in the second stage reaction is controlled by nucleation and growth. The nucleation and growth of Li and Fe sulfates in the third stage not only occur at this stage, but their rates are also controlled by diffusion. The dynamic equations for the second and third stages are as follows:
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