{"title":"利用Ru催化剂和熔融氢氧化物电解质的透氢膜电化学电池,利用电从水和氮合成氨:与氨分离和未反应气体再循环相结合†","authors":"Raisei Sagara, Eriko Watanabe and Jun Kubota","doi":"10.1039/D5SE00348B","DOIUrl":null,"url":null,"abstract":"<p >There is considerable interest in synthesizing NH<small><sub>3</sub></small> directly from abundant H<small><sub>2</sub></small>O and N<small><sub>2</sub></small> using electricity from renewable energy sources, for applications such as synthetic fuels, artificial fertilizers, and raw materials for plastics. NH<small><sub>3</sub></small> synthesis from N<small><sub>2</sub></small> and H<small><sub>2</sub></small>O was investigated using an electrochemical setup featuring Ru/Cs<small><sup>+</sup></small>/C catalysts, Pd alloy membrane cathodes, NaOH–KOH molten electrolytes, and Ni anodes operated at 250 °C and 1.0 MPa (absolute). This electrochemical setup was integrated with a refrigerated gas/liquid separator at −75 °C to concentrate NH<small><sub>3</sub></small> and a recirculation pump for unreacted H<small><sub>2</sub></small> and N<small><sub>2</sub></small>. As a single-pass reactor, if NH<small><sub>3</sub></small> separation and unreacted gas recirculation were not used, this electrochemical device produced NH<small><sub>3</sub></small> at 1.0 MPa and 250 °C, with an apparent current efficiency of 32–20% at 10–100 mA cm<small><sup>−2</sup></small>. This efficiency was limited by the chemical equilibrium, which is calculated to be 36%. The study achieved a 90% apparent current efficiency, with a 320 nmol s<small><sup>−1</sup></small> cm<small><sup>−2</sup></small> production rate of NH<small><sub>3</sub></small> at 100 mA cm<small><sup>−2</sup></small>, 250 °C, and 1.0 MPa with NH<small><sub>3</sub></small> separation and unreacted gas recirculation. The remaining 10% of the apparent current efficiency was used for H<small><sub>2</sub></small> production. The reaction kinetic properties and scalability of the present system were discussed.</p>","PeriodicalId":104,"journal":{"name":"Sustainable Energy & Fuels","volume":" 10","pages":" 2658-2669"},"PeriodicalIF":5.0000,"publicationDate":"2025-04-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.rsc.org/en/content/articlepdf/2025/se/d5se00348b?page=search","citationCount":"0","resultStr":"{\"title\":\"Ammonia synthesis from water and nitrogen using electricity with a hydrogen-permeable membrane electrochemical cell with Ru catalysts and molten hydroxide electrolyte: integration with ammonia separation and unreacted gas recirculation†\",\"authors\":\"Raisei Sagara, Eriko Watanabe and Jun Kubota\",\"doi\":\"10.1039/D5SE00348B\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p >There is considerable interest in synthesizing NH<small><sub>3</sub></small> directly from abundant H<small><sub>2</sub></small>O and N<small><sub>2</sub></small> using electricity from renewable energy sources, for applications such as synthetic fuels, artificial fertilizers, and raw materials for plastics. NH<small><sub>3</sub></small> synthesis from N<small><sub>2</sub></small> and H<small><sub>2</sub></small>O was investigated using an electrochemical setup featuring Ru/Cs<small><sup>+</sup></small>/C catalysts, Pd alloy membrane cathodes, NaOH–KOH molten electrolytes, and Ni anodes operated at 250 °C and 1.0 MPa (absolute). This electrochemical setup was integrated with a refrigerated gas/liquid separator at −75 °C to concentrate NH<small><sub>3</sub></small> and a recirculation pump for unreacted H<small><sub>2</sub></small> and N<small><sub>2</sub></small>. As a single-pass reactor, if NH<small><sub>3</sub></small> separation and unreacted gas recirculation were not used, this electrochemical device produced NH<small><sub>3</sub></small> at 1.0 MPa and 250 °C, with an apparent current efficiency of 32–20% at 10–100 mA cm<small><sup>−2</sup></small>. This efficiency was limited by the chemical equilibrium, which is calculated to be 36%. The study achieved a 90% apparent current efficiency, with a 320 nmol s<small><sup>−1</sup></small> cm<small><sup>−2</sup></small> production rate of NH<small><sub>3</sub></small> at 100 mA cm<small><sup>−2</sup></small>, 250 °C, and 1.0 MPa with NH<small><sub>3</sub></small> separation and unreacted gas recirculation. The remaining 10% of the apparent current efficiency was used for H<small><sub>2</sub></small> production. 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引用次数: 0
摘要
利用来自可再生能源的电力,从丰富的H2O和N2中直接合成NH3,用于合成燃料、人造肥料和塑料原料,这是一个相当大的兴趣。采用Ru/Cs+/C催化剂、Pd合金膜阴极、NaOH-KOH熔融电解质和Ni阳极,在250℃和1.0 MPa(绝对温度)下,研究了N2和H2O合成NH3的电化学设置。该电化学装置集成了- 75°C的冷冻气/液分离器,用于浓缩NH3,再循环泵用于未反应的H2和N2。该电化学装置为单道反应器,在不进行NH3分离和未反应气体再循环的情况下,在1.0 MPa和250℃条件下产生NH3,在10-100 mA cm−2条件下,表观电流效率为32-20%。该效率受到化学平衡的限制,计算结果为36%。在分离NH3和未反应气体再循环的条件下,在100 mA cm - 2、250℃、1.0 MPa条件下,NH3的产率为320 nmol s - 1 cm - 2,表观电流效率达到90%。剩余10%的视电流效率用于制氢。讨论了该体系的反应动力学性质和可扩展性。
Ammonia synthesis from water and nitrogen using electricity with a hydrogen-permeable membrane electrochemical cell with Ru catalysts and molten hydroxide electrolyte: integration with ammonia separation and unreacted gas recirculation†
There is considerable interest in synthesizing NH3 directly from abundant H2O and N2 using electricity from renewable energy sources, for applications such as synthetic fuels, artificial fertilizers, and raw materials for plastics. NH3 synthesis from N2 and H2O was investigated using an electrochemical setup featuring Ru/Cs+/C catalysts, Pd alloy membrane cathodes, NaOH–KOH molten electrolytes, and Ni anodes operated at 250 °C and 1.0 MPa (absolute). This electrochemical setup was integrated with a refrigerated gas/liquid separator at −75 °C to concentrate NH3 and a recirculation pump for unreacted H2 and N2. As a single-pass reactor, if NH3 separation and unreacted gas recirculation were not used, this electrochemical device produced NH3 at 1.0 MPa and 250 °C, with an apparent current efficiency of 32–20% at 10–100 mA cm−2. This efficiency was limited by the chemical equilibrium, which is calculated to be 36%. The study achieved a 90% apparent current efficiency, with a 320 nmol s−1 cm−2 production rate of NH3 at 100 mA cm−2, 250 °C, and 1.0 MPa with NH3 separation and unreacted gas recirculation. The remaining 10% of the apparent current efficiency was used for H2 production. The reaction kinetic properties and scalability of the present system were discussed.
期刊介绍:
Sustainable Energy & Fuels will publish research that contributes to the development of sustainable energy technologies with a particular emphasis on new and next-generation technologies.