{"title":"在阴极混凝-阳极氧化协同体系中,pH自缓冲效应介导铵离子电氯化制N2的强化","authors":"Xuanzhen Ren, Shuzhen Li, Xiangru Ren, Yifan Li, Qipeng Yang, Pei Dong, Bo Jiang","doi":"10.1016/j.seppur.2025.133679","DOIUrl":null,"url":null,"abstract":"<div><div>Electrochlorination of NH<sub>4</sub><sup>+</sup> to N<sub>2</sub> has been widely used for wastewater treatment, but it suffers from inefficiency because of the solution acidification caused by the protons releasing from NH<sub>4</sub><sup>+</sup>-N oxidation. This study developed an electrochemical NH<sub>4</sub><sup>+</sup>-N oxidation system employing Al cathode paired with an IrO<sub>2</sub>-RuO<sub>2</sub>/Ti anode, where the acidification effect could be effectively spontaneously alleviated by the hydroxyl-aluminum species produced during the reaction. The solution pH maintained 5.1 and gradually increased to 7 after 120 min. In contrast, the solution pH dropped below 3 when SS or Ni foam was used as the cathode. The NH<sub>4</sub><sup>+</sup>-N oxidation system with Al cathode showed NH<sub>4</sub><sup>+</sup>-N oxidation efficiency of 99% at a current density of 20 mA cm<sup>−2</sup> and Cl<sup>-</sup> concentration of 30 mM, which outperformed the systems with Ni foam (20 %) and SS cathode (67 %). Additionally, the NH<sub>4</sub><sup>+</sup>-N oxidation system with Al cathode had appreciable resistance to organic pollutants, achieving 90 % COD removal efficiency while maintaining high NH<sub>4</sub><sup>+</sup>-N oxidation efficiency (88 %), which was much higher than SS (23 %) and Ni foam cathode (13.7 %). The NH<sub>4</sub><sup>+</sup>-N oxidation efficiency decreased 12 % by the addition of TBA to remove the Cl<sup>•</sup> and OH<sup>•</sup>. This result indicates that the free chlorine was the primary oxidizing species for NH<sub>4</sub><sup>+</sup>-N oxidation and could be well utilized to oxidize NH<sub>4</sub><sup>+</sup> to N<sub>2</sub> at nearly neutral pH spontaneously regulated by cathode coagulation reactions. This study offers a promising method for NH<sub>4</sub><sup>+</sup>-N wastewater treatment and promotes the industrial application.</div></div>","PeriodicalId":427,"journal":{"name":"Separation and Purification Technology","volume":"374 ","pages":"Article 133679"},"PeriodicalIF":8.1000,"publicationDate":"2025-05-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Enhanced electrochlorination of ammonium to N2 mediated by pH self-buffering effect in the cathodic coagulation and anodic oxidation synergistic system\",\"authors\":\"Xuanzhen Ren, Shuzhen Li, Xiangru Ren, Yifan Li, Qipeng Yang, Pei Dong, Bo Jiang\",\"doi\":\"10.1016/j.seppur.2025.133679\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>Electrochlorination of NH<sub>4</sub><sup>+</sup> to N<sub>2</sub> has been widely used for wastewater treatment, but it suffers from inefficiency because of the solution acidification caused by the protons releasing from NH<sub>4</sub><sup>+</sup>-N oxidation. This study developed an electrochemical NH<sub>4</sub><sup>+</sup>-N oxidation system employing Al cathode paired with an IrO<sub>2</sub>-RuO<sub>2</sub>/Ti anode, where the acidification effect could be effectively spontaneously alleviated by the hydroxyl-aluminum species produced during the reaction. The solution pH maintained 5.1 and gradually increased to 7 after 120 min. In contrast, the solution pH dropped below 3 when SS or Ni foam was used as the cathode. The NH<sub>4</sub><sup>+</sup>-N oxidation system with Al cathode showed NH<sub>4</sub><sup>+</sup>-N oxidation efficiency of 99% at a current density of 20 mA cm<sup>−2</sup> and Cl<sup>-</sup> concentration of 30 mM, which outperformed the systems with Ni foam (20 %) and SS cathode (67 %). Additionally, the NH<sub>4</sub><sup>+</sup>-N oxidation system with Al cathode had appreciable resistance to organic pollutants, achieving 90 % COD removal efficiency while maintaining high NH<sub>4</sub><sup>+</sup>-N oxidation efficiency (88 %), which was much higher than SS (23 %) and Ni foam cathode (13.7 %). The NH<sub>4</sub><sup>+</sup>-N oxidation efficiency decreased 12 % by the addition of TBA to remove the Cl<sup>•</sup> and OH<sup>•</sup>. This result indicates that the free chlorine was the primary oxidizing species for NH<sub>4</sub><sup>+</sup>-N oxidation and could be well utilized to oxidize NH<sub>4</sub><sup>+</sup> to N<sub>2</sub> at nearly neutral pH spontaneously regulated by cathode coagulation reactions. This study offers a promising method for NH<sub>4</sub><sup>+</sup>-N wastewater treatment and promotes the industrial application.</div></div>\",\"PeriodicalId\":427,\"journal\":{\"name\":\"Separation and Purification Technology\",\"volume\":\"374 \",\"pages\":\"Article 133679\"},\"PeriodicalIF\":8.1000,\"publicationDate\":\"2025-05-23\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Separation and Purification Technology\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S1383586625022762\",\"RegionNum\":1,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Separation and Purification Technology","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1383586625022762","RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
摘要
NH4+电氯化制N2已被广泛应用于污水处理,但由于NH4+-N氧化释放的质子导致溶液酸化,导致效率低下。本研究采用Al阴极与IrO2-RuO2/Ti阳极配对,开发了一种电化学NH4+-N氧化体系,反应过程中产生的羟基铝物质可以有效地自发减轻酸化效应。溶液pH维持在5.1,120 min后逐渐升高到7,而以SS或Ni泡沫为阴极时,溶液pH降至3以下。以Al为阴极的NH4+- n氧化体系在电流密度为20 mA cm−2、Cl-浓度为30 mM时的NH4+- n氧化效率为99%,优于泡沫镍(20%)和SS为阴极(67%)的体系。此外,Al阴极的NH4+-N氧化体系对有机污染物具有明显的抗性,COD去除率达到90%,NH4+-N氧化效率高达88%,远高于SS(23%)和Ni泡沫阴极(13.7%)。通过添加TBA去除Cl•和OH•,NH4+-N的氧化效率降低了12%。这表明游离氯是NH4+-N氧化的主要氧化物质,可以很好地利用阴极凝聚反应在接近中性的pH下将NH4+自发氧化成N2。该研究为NH4+-N废水处理提供了一种有前景的方法,并促进了工业应用。
Enhanced electrochlorination of ammonium to N2 mediated by pH self-buffering effect in the cathodic coagulation and anodic oxidation synergistic system
Electrochlorination of NH4+ to N2 has been widely used for wastewater treatment, but it suffers from inefficiency because of the solution acidification caused by the protons releasing from NH4+-N oxidation. This study developed an electrochemical NH4+-N oxidation system employing Al cathode paired with an IrO2-RuO2/Ti anode, where the acidification effect could be effectively spontaneously alleviated by the hydroxyl-aluminum species produced during the reaction. The solution pH maintained 5.1 and gradually increased to 7 after 120 min. In contrast, the solution pH dropped below 3 when SS or Ni foam was used as the cathode. The NH4+-N oxidation system with Al cathode showed NH4+-N oxidation efficiency of 99% at a current density of 20 mA cm−2 and Cl- concentration of 30 mM, which outperformed the systems with Ni foam (20 %) and SS cathode (67 %). Additionally, the NH4+-N oxidation system with Al cathode had appreciable resistance to organic pollutants, achieving 90 % COD removal efficiency while maintaining high NH4+-N oxidation efficiency (88 %), which was much higher than SS (23 %) and Ni foam cathode (13.7 %). The NH4+-N oxidation efficiency decreased 12 % by the addition of TBA to remove the Cl• and OH•. This result indicates that the free chlorine was the primary oxidizing species for NH4+-N oxidation and could be well utilized to oxidize NH4+ to N2 at nearly neutral pH spontaneously regulated by cathode coagulation reactions. This study offers a promising method for NH4+-N wastewater treatment and promotes the industrial application.
期刊介绍:
Separation and Purification Technology is a premier journal committed to sharing innovative methods for separation and purification in chemical and environmental engineering, encompassing both homogeneous solutions and heterogeneous mixtures. Our scope includes the separation and/or purification of liquids, vapors, and gases, as well as carbon capture and separation techniques. However, it's important to note that methods solely intended for analytical purposes are not within the scope of the journal. Additionally, disciplines such as soil science, polymer science, and metallurgy fall outside the purview of Separation and Purification Technology. Join us in advancing the field of separation and purification methods for sustainable solutions in chemical and environmental engineering.