{"title":"利用低氧势铁氧体进行化学循环高炉煤气脱碳:工艺和热力学分析","authors":"Made Santihayu Sukma, Stuart Ashley Scott","doi":"10.1016/j.ijggc.2024.104240","DOIUrl":null,"url":null,"abstract":"<div><p>Previous work demonstrated Ca<sub>2</sub>Fe<sub>2</sub>O<sub>5</sub> (C<sub>2</sub>F) can react in a blast furnace gas (BFG) with <span><math><mrow><msub><mi>P</mi><mtext>CO</mtext></msub><mo>/</mo><msub><mi>P</mi><mrow><mi>C</mi><msub><mi>O</mi><mn>2</mn></msub></mrow></msub></mrow></math></span> ratio of ∼1, despite of its reduction to CaO + Fe requiring a ratio of ∼3. This is possible due to the interaction with carbonation and the formation of other iron containing phases. Here, the proposed calcium and chemical looping combustion using C<sub>2</sub>F was examined using process modelling in ASPEN Plus and MTDATA. The low chemical potential of oxygen in C<sub>2</sub>F allows CO/H<sub>2</sub> combustion to be endothermic in the lower temperature carbonator (particularly when reducing to Fe<sub>x</sub>O), leading to a more exothermic reaction during oxidation in the higher temperature calciner. In this scheme, the heat of BFG combustion is chemically pumped from the lower temperature carbonator to the higher temperature calciner using the looping material, reducing the energy use in the calciner by around 40 kW/mol-BFG compared to the calcium looping alone or to the calcium copper looping. The reincorporation of CaO and Fe/Fe<sub>x</sub>O into C<sub>2</sub>F would allow the calcination temperature to be lowered to 770 °C (compared with calcium looping, which requires ∼ 900 °C), and the system can be entirely autothermal.</p></div>","PeriodicalId":334,"journal":{"name":"International Journal of Greenhouse Gas Control","volume":"138 ","pages":"Article 104240"},"PeriodicalIF":4.6000,"publicationDate":"2024-09-11","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S175058362400183X/pdfft?md5=47b429d31805171a916ba07ee15cd6d7&pid=1-s2.0-S175058362400183X-main.pdf","citationCount":"0","resultStr":"{\"title\":\"Decarbonising blast furnace gas with chemical looping using low oxygen potential ferrites: process and thermodynamic analysis\",\"authors\":\"Made Santihayu Sukma, Stuart Ashley Scott\",\"doi\":\"10.1016/j.ijggc.2024.104240\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>Previous work demonstrated Ca<sub>2</sub>Fe<sub>2</sub>O<sub>5</sub> (C<sub>2</sub>F) can react in a blast furnace gas (BFG) with <span><math><mrow><msub><mi>P</mi><mtext>CO</mtext></msub><mo>/</mo><msub><mi>P</mi><mrow><mi>C</mi><msub><mi>O</mi><mn>2</mn></msub></mrow></msub></mrow></math></span> ratio of ∼1, despite of its reduction to CaO + Fe requiring a ratio of ∼3. This is possible due to the interaction with carbonation and the formation of other iron containing phases. Here, the proposed calcium and chemical looping combustion using C<sub>2</sub>F was examined using process modelling in ASPEN Plus and MTDATA. The low chemical potential of oxygen in C<sub>2</sub>F allows CO/H<sub>2</sub> combustion to be endothermic in the lower temperature carbonator (particularly when reducing to Fe<sub>x</sub>O), leading to a more exothermic reaction during oxidation in the higher temperature calciner. In this scheme, the heat of BFG combustion is chemically pumped from the lower temperature carbonator to the higher temperature calciner using the looping material, reducing the energy use in the calciner by around 40 kW/mol-BFG compared to the calcium looping alone or to the calcium copper looping. The reincorporation of CaO and Fe/Fe<sub>x</sub>O into C<sub>2</sub>F would allow the calcination temperature to be lowered to 770 °C (compared with calcium looping, which requires ∼ 900 °C), and the system can be entirely autothermal.</p></div>\",\"PeriodicalId\":334,\"journal\":{\"name\":\"International Journal of Greenhouse Gas Control\",\"volume\":\"138 \",\"pages\":\"Article 104240\"},\"PeriodicalIF\":4.6000,\"publicationDate\":\"2024-09-11\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://www.sciencedirect.com/science/article/pii/S175058362400183X/pdfft?md5=47b429d31805171a916ba07ee15cd6d7&pid=1-s2.0-S175058362400183X-main.pdf\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"International Journal of Greenhouse Gas Control\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S175058362400183X\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENERGY & FUELS\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Journal of Greenhouse Gas Control","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S175058362400183X","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0
摘要
之前的研究表明,尽管 Ca2Fe2O5(C2F)还原成 CaO + Fe 的比率需要 ∼3,但它可以在 PCO/PCO2 比率为 ∼1 的高炉煤气(BFG)中发生反应。这可能是由于碳化作用和其他含铁相的形成。在此,我们利用 ASPEN Plus 和 MTDATA 的过程建模,对利用 C2F 进行钙和化学循环燃烧的建议进行了研究。C2F 中氧的化学势较低,使得 CO/H2 燃烧在较低温度的碳化炉中(特别是还原成 FexO 时)产生内热,从而在较高温度的煅烧炉中氧化过程中产生更多放热反应。在这种方案中,BFG 燃烧的热量通过化学泵从温度较低的碳化炉利用循环材料输送到温度较高的煅烧炉,与单独的钙循环或钙铜循环相比,煅烧炉的能耗降低了约 40 kW/mol-BFG。将 CaO 和 Fe/FexO 重新并入 C2F 可使煅烧温度降低到 770 °C(与钙循环相比,钙循环需要 900 °C),而且该系统可以完全自热。
Decarbonising blast furnace gas with chemical looping using low oxygen potential ferrites: process and thermodynamic analysis
Previous work demonstrated Ca2Fe2O5 (C2F) can react in a blast furnace gas (BFG) with ratio of ∼1, despite of its reduction to CaO + Fe requiring a ratio of ∼3. This is possible due to the interaction with carbonation and the formation of other iron containing phases. Here, the proposed calcium and chemical looping combustion using C2F was examined using process modelling in ASPEN Plus and MTDATA. The low chemical potential of oxygen in C2F allows CO/H2 combustion to be endothermic in the lower temperature carbonator (particularly when reducing to FexO), leading to a more exothermic reaction during oxidation in the higher temperature calciner. In this scheme, the heat of BFG combustion is chemically pumped from the lower temperature carbonator to the higher temperature calciner using the looping material, reducing the energy use in the calciner by around 40 kW/mol-BFG compared to the calcium looping alone or to the calcium copper looping. The reincorporation of CaO and Fe/FexO into C2F would allow the calcination temperature to be lowered to 770 °C (compared with calcium looping, which requires ∼ 900 °C), and the system can be entirely autothermal.
期刊介绍:
The International Journal of Greenhouse Gas Control is a peer reviewed journal focusing on scientific and engineering developments in greenhouse gas control through capture and storage at large stationary emitters in the power sector and in other major resource, manufacturing and production industries. The Journal covers all greenhouse gas emissions within the power and industrial sectors, and comprises both technical and non-technical related literature in one volume. Original research, review and comments papers are included.