Dydia Tanisha González, José Alberto Baeza*, Luisa Calvo and Miguel Ángel Gilarranz,
{"title":"高浓度含硝酸盐工业废水的催化还原回收铵","authors":"Dydia Tanisha González, José Alberto Baeza*, Luisa Calvo and Miguel Ángel Gilarranz, ","doi":"10.1021/acsestwater.4c0089710.1021/acsestwater.4c00897","DOIUrl":null,"url":null,"abstract":"<p >The concept of NH<sub>4</sub><sup>+</sup>/NH<sub>3</sub> production from wastewater treatment for subsequent recovery and reuse has gained much attention in the past few years. The conversion of NO<sub>3</sub><sup>–</sup> present in wastewater into NH<sub>4</sub><sup>+</sup>/NH<sub>3</sub> through catalytic reduction is a sustainable approach for resource utilization from wastewater. In the present work, the application of this technique to industrial wastewater with a high NO<sub>3</sub><sup>–</sup> concentration is proposed. A good activity of Pd–Cu catalysts supported on carbon black was observed at high NO<sub>3</sub><sup>–</sup> concentrations. Complete NO<sub>3</sub><sup>–</sup> conversion was achieved in water with an initial concentration of 1000 mg/L and a catalyst concentration of 0.93 g/L in a stirred reactor. Furthermore, an improvement in catalytic activity was obtained when the reactor was operated without pH control, resulting in an increase in NH<sub>4</sub><sup>+</sup> formation to 184 mg/L. Additionally, in successive 8-h reaction cycles with a reaction medium equivalent to that of industrial wastewater, a progressive decrease in catalytic activity was observed, which may be associated with a noticeable decrease in the Pd<sup>0</sup>/Pd<sup>n+</sup> species ratio.</p>","PeriodicalId":93847,"journal":{"name":"ACS ES&T water","volume":"5 4","pages":"1595–1604 1595–1604"},"PeriodicalIF":4.8000,"publicationDate":"2025-03-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Catalytic Reduction of High Concentration Nitrate-Bearing Industrial Wastewater for Ammonium Recovery\",\"authors\":\"Dydia Tanisha González, José Alberto Baeza*, Luisa Calvo and Miguel Ángel Gilarranz, \",\"doi\":\"10.1021/acsestwater.4c0089710.1021/acsestwater.4c00897\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p >The concept of NH<sub>4</sub><sup>+</sup>/NH<sub>3</sub> production from wastewater treatment for subsequent recovery and reuse has gained much attention in the past few years. The conversion of NO<sub>3</sub><sup>–</sup> present in wastewater into NH<sub>4</sub><sup>+</sup>/NH<sub>3</sub> through catalytic reduction is a sustainable approach for resource utilization from wastewater. In the present work, the application of this technique to industrial wastewater with a high NO<sub>3</sub><sup>–</sup> concentration is proposed. A good activity of Pd–Cu catalysts supported on carbon black was observed at high NO<sub>3</sub><sup>–</sup> concentrations. Complete NO<sub>3</sub><sup>–</sup> conversion was achieved in water with an initial concentration of 1000 mg/L and a catalyst concentration of 0.93 g/L in a stirred reactor. Furthermore, an improvement in catalytic activity was obtained when the reactor was operated without pH control, resulting in an increase in NH<sub>4</sub><sup>+</sup> formation to 184 mg/L. Additionally, in successive 8-h reaction cycles with a reaction medium equivalent to that of industrial wastewater, a progressive decrease in catalytic activity was observed, which may be associated with a noticeable decrease in the Pd<sup>0</sup>/Pd<sup>n+</sup> species ratio.</p>\",\"PeriodicalId\":93847,\"journal\":{\"name\":\"ACS ES&T water\",\"volume\":\"5 4\",\"pages\":\"1595–1604 1595–1604\"},\"PeriodicalIF\":4.8000,\"publicationDate\":\"2025-03-19\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"ACS ES&T water\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://pubs.acs.org/doi/10.1021/acsestwater.4c00897\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENVIRONMENTAL SCIENCES\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"ACS ES&T water","FirstCategoryId":"1085","ListUrlMain":"https://pubs.acs.org/doi/10.1021/acsestwater.4c00897","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENVIRONMENTAL SCIENCES","Score":null,"Total":0}
Catalytic Reduction of High Concentration Nitrate-Bearing Industrial Wastewater for Ammonium Recovery
The concept of NH4+/NH3 production from wastewater treatment for subsequent recovery and reuse has gained much attention in the past few years. The conversion of NO3– present in wastewater into NH4+/NH3 through catalytic reduction is a sustainable approach for resource utilization from wastewater. In the present work, the application of this technique to industrial wastewater with a high NO3– concentration is proposed. A good activity of Pd–Cu catalysts supported on carbon black was observed at high NO3– concentrations. Complete NO3– conversion was achieved in water with an initial concentration of 1000 mg/L and a catalyst concentration of 0.93 g/L in a stirred reactor. Furthermore, an improvement in catalytic activity was obtained when the reactor was operated without pH control, resulting in an increase in NH4+ formation to 184 mg/L. Additionally, in successive 8-h reaction cycles with a reaction medium equivalent to that of industrial wastewater, a progressive decrease in catalytic activity was observed, which may be associated with a noticeable decrease in the Pd0/Pdn+ species ratio.