{"title":"一体化制造双金属 PdIn 涂层多孔聚醚砜膜,用于催化甲酸将水中的 NO3 还原成 NH3","authors":"Marcus Ropertz , Mathias Ulbricht , Lukas Fischer","doi":"10.1016/j.ceja.2024.100683","DOIUrl":null,"url":null,"abstract":"<div><div>We utilized a novel <em>all-in-one</em> method to fabricate porous polyethersulfone (PES) membranes containing bimetallic PdIn as catalyst and a cationic ionomer to introduce charged surface groups. Our fabrication is based on <em>in situ</em> solidification of dissolved palladium and indium ions in a PES-ionomer casting-reaction solution, directly followed by preparation of porous catalytic membranes through film casting and phase separation in water. We employed as-prepared membranes in the catalytic reduction of NO<sub>3</sub><sup>−</sup> (50 mg/L, 0.81 mM) to NH<sub>3</sub> in water using formic acid (FA) as electron source. The <em>in situ</em> solidification of PdCl<sub>4</sub><sup>2−</sup> and In<sup>3+</sup> generated PdIn species with the highest catalytic activity, compared to Pd<sup>2+</sup> and In<sup>3+</sup> or a sequential solidification of Pd followed by In. Moreover, positively charged ionomer in a Pd<sub>3</sub>In<sub>1</sub>-PES membrane boosted NO<sub>3</sub><sup>−</sup> conversion rate in flow-through at pH 7 from 2.5 to 17 mmol/m<sup>2</sup>h and NH<sub>3</sub> selectivity from 4 % to 34 %, likely by promoting interaction between nitrate and formate anions with catalyst sites. Reducing the flow rate from 100 to 50 L/m<sup>2</sup>h further enhanced NH<sub>3</sub> selectivity to 55 % (NH<sub>3</sub> production rate of 189 µg/h mg), illustrating that a longer residence time in the membrane promotes NH<sub>3</sub> formation. Additionally, we achieved 90 % electron efficiency for NO<sub>3</sub><sup>−</sup> reduction with FA in flow-through compared to 60 % in batch, highlighting that a short contact time between catalyst and FA limits excess consumption through dehydrogenation. Finally, we demonstrated continuous NH<sub>3</sub> production from NO<sub>3</sub><sup>−</sup> for 11 h of flow-through, and found indications that PdIn catalyzes NO<sub>3</sub><sup>−</sup> reduction through an electron/oxygen transfer cycle.</div></div>","PeriodicalId":9749,"journal":{"name":"Chemical Engineering Journal Advances","volume":"20 ","pages":"Article 100683"},"PeriodicalIF":5.5000,"publicationDate":"2024-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"All-in-one fabrication of bimetallic PdIn-decorated porous PES membranes for the catalytic flow-through reduction of NO3− to NH3 with formic acid in water\",\"authors\":\"Marcus Ropertz , Mathias Ulbricht , Lukas Fischer\",\"doi\":\"10.1016/j.ceja.2024.100683\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>We utilized a novel <em>all-in-one</em> method to fabricate porous polyethersulfone (PES) membranes containing bimetallic PdIn as catalyst and a cationic ionomer to introduce charged surface groups. Our fabrication is based on <em>in situ</em> solidification of dissolved palladium and indium ions in a PES-ionomer casting-reaction solution, directly followed by preparation of porous catalytic membranes through film casting and phase separation in water. We employed as-prepared membranes in the catalytic reduction of NO<sub>3</sub><sup>−</sup> (50 mg/L, 0.81 mM) to NH<sub>3</sub> in water using formic acid (FA) as electron source. The <em>in situ</em> solidification of PdCl<sub>4</sub><sup>2−</sup> and In<sup>3+</sup> generated PdIn species with the highest catalytic activity, compared to Pd<sup>2+</sup> and In<sup>3+</sup> or a sequential solidification of Pd followed by In. Moreover, positively charged ionomer in a Pd<sub>3</sub>In<sub>1</sub>-PES membrane boosted NO<sub>3</sub><sup>−</sup> conversion rate in flow-through at pH 7 from 2.5 to 17 mmol/m<sup>2</sup>h and NH<sub>3</sub> selectivity from 4 % to 34 %, likely by promoting interaction between nitrate and formate anions with catalyst sites. Reducing the flow rate from 100 to 50 L/m<sup>2</sup>h further enhanced NH<sub>3</sub> selectivity to 55 % (NH<sub>3</sub> production rate of 189 µg/h mg), illustrating that a longer residence time in the membrane promotes NH<sub>3</sub> formation. Additionally, we achieved 90 % electron efficiency for NO<sub>3</sub><sup>−</sup> reduction with FA in flow-through compared to 60 % in batch, highlighting that a short contact time between catalyst and FA limits excess consumption through dehydrogenation. Finally, we demonstrated continuous NH<sub>3</sub> production from NO<sub>3</sub><sup>−</sup> for 11 h of flow-through, and found indications that PdIn catalyzes NO<sub>3</sub><sup>−</sup> reduction through an electron/oxygen transfer cycle.</div></div>\",\"PeriodicalId\":9749,\"journal\":{\"name\":\"Chemical Engineering Journal Advances\",\"volume\":\"20 \",\"pages\":\"Article 100683\"},\"PeriodicalIF\":5.5000,\"publicationDate\":\"2024-11-15\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical Engineering Journal Advances\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S2666821124001005\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering Journal Advances","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2666821124001005","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
All-in-one fabrication of bimetallic PdIn-decorated porous PES membranes for the catalytic flow-through reduction of NO3− to NH3 with formic acid in water
We utilized a novel all-in-one method to fabricate porous polyethersulfone (PES) membranes containing bimetallic PdIn as catalyst and a cationic ionomer to introduce charged surface groups. Our fabrication is based on in situ solidification of dissolved palladium and indium ions in a PES-ionomer casting-reaction solution, directly followed by preparation of porous catalytic membranes through film casting and phase separation in water. We employed as-prepared membranes in the catalytic reduction of NO3− (50 mg/L, 0.81 mM) to NH3 in water using formic acid (FA) as electron source. The in situ solidification of PdCl42− and In3+ generated PdIn species with the highest catalytic activity, compared to Pd2+ and In3+ or a sequential solidification of Pd followed by In. Moreover, positively charged ionomer in a Pd3In1-PES membrane boosted NO3− conversion rate in flow-through at pH 7 from 2.5 to 17 mmol/m2h and NH3 selectivity from 4 % to 34 %, likely by promoting interaction between nitrate and formate anions with catalyst sites. Reducing the flow rate from 100 to 50 L/m2h further enhanced NH3 selectivity to 55 % (NH3 production rate of 189 µg/h mg), illustrating that a longer residence time in the membrane promotes NH3 formation. Additionally, we achieved 90 % electron efficiency for NO3− reduction with FA in flow-through compared to 60 % in batch, highlighting that a short contact time between catalyst and FA limits excess consumption through dehydrogenation. Finally, we demonstrated continuous NH3 production from NO3− for 11 h of flow-through, and found indications that PdIn catalyzes NO3− reduction through an electron/oxygen transfer cycle.