铁基载氧体在煤化学链燃烧中的热力学循环模拟

Thermodynamic cycle simulation of iron-based oxygen carriers in coal chemical looping combustion

  • 摘要: 化学链燃烧(Chemical Looping Combustion, CLC)作为一种高效的碳捕集技术,通过利用载氧体在氧化还原循环中的反应特性,实现了化石燃料燃烧过程中CO2的高效捕集和分离。采用Cantera模拟软件,对铁基载氧体在煤化学链(Coal Direct Chemical Looping, CDCL)燃烧中的氧化还原循环进行了热力学模拟,系统研究了载氧体的损耗特性、循环性能对反应生成物的影响。结果表明,在设定的模拟条件下,循环次数最多为388次,在前120次循环中,载氧体以Fe3O4和FeO为主,具有较强的氧化能力,与燃料反应生成以CO2和H2O为主的气态产物。随着循环次数增加至270次,载氧体逐步还原至低氧化态(Fe),氧化能力下降,还原反应占主导,生成更多的CO和H2,产物分布呈现出阶段性变化。之后的循环中,载氧体的氧化能力显著下降,固体损耗趋于平稳。此外,引入了基于能量调控的动态损耗机制,发现能量利用效率显著影响循环次数和反应平衡,能量差与固体损耗呈正相关。模拟结果显示,燃料反应器中,循环初期的能量差最高可达3.35×105 kJ/mol,随着反应的深入逐步下降并趋于平衡;空气反应器中,循环初期的能量差最高可达3.72×105 kJ/mol,氧化反应效率在初期较高,但随后逐步下降并接近平稳状态。从多次循环中的能量差出发,结合固态及气态产物的分布,为铁基载氧体在CDCL燃烧技术中的寿命评估和优化设计提供了思路。

     

    Abstract: Chemical Looping Combustion (CLC) is recognized as an efficient carbon capture technology, achieving high CO2 capture and separation during fossil fuel combustion by utilizing the redox properties of oxygen carriers in redox cycles. The redox cycles of iron-based oxygen carriers in Coal Direct Chemical Looping (CDCL) combustion were thermodynamically simulated using Cantera software. The loss characteristics of the oxygen carriers and the effects of cycle performance on reaction products were systematically studied. Under the defined simulation conditions, the maximum number of cycles reached 388. In the first 120 cycles, the oxygen carriers are primarily composed of Fe3O4 and FeO, exhibiting strong oxidation capabilities and reacting with the fuel to produce gas-phase products dominated by CO2 and H2O. As the number of cycles increases to 270, the oxygen carriers are gradually reduced to a lower oxidation state (Fe), leading to a decrease in oxidation capacity, with reduction reactions dominating and generating more CO and H2, resulting in staged changes in product distribution. In subsequent cycles, the oxidation capacity of the oxygen carriers significantly declines, and solid loss stabilizes. Additionally, a dynamic loss mechanism based on energy regulation is introduced, showing that energy utilization efficiency significantly impacts the number of cycles and reaction equilibrium, with a positive correlation observed between energy difference and solid loss. The simulation results indicate that in the fuel reactor, the energy difference initially reaches up to 3.35×105 kJ/ mol, then gradually decreases and approaches equilibrium as the reaction progresses. In the air reactor, the energy difference initially peaks at 3.72×105 kJ/ mol, with high oxidation reaction efficiency at the beginning, which then gradually decreases and approaches a steady state. By analyzing the energy differences over multiple cycles along with the distribution of solid and gas-phase products, insights are provided for the lifespan assessment and optimization design of iron-based oxygen carriers in CDCL combustion technology.

     

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