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    基于Aspen Plus的自供热式吸附强化生物质气化制氢

    Hydrogen production from self-heating adsorption-enhanced biomass gasification based on Aspen Plus

    • 摘要: 在“双碳”背景下,生物质能作为可再生能源的关键组成部分,逐渐成为实现碳中和目标的重要技术路径。自供热式吸附强化生物质气化(SSEG)作为一种新兴的气化技术,通过吸附与气化的协同作用,在提高氢气生产效率和减少碳排放方面表现出显著的优势。因此,自供热式吸附强化生物质气化与蒸汽重整耦合(SSEG−SR)工艺被提出。利用Aspen Plus软件对该工艺进行建模与仿真,采用吉布斯反应器对气化与重整过程进行热力学建模,并结合Peng-Robinson立方状态方程和Boston-Mathias函数进行物性估算,从物料流、能量流、经济性及环境影响等方面对SSEG−SR工艺链进行了全面分析。通过与现有试验数据和工业运营数据的对比,验证了模型构建的准确性和可靠性。物料流分析结果表明:生产1 t氢气SSEG−SR工艺需消耗7.63 t生物质原料,氢气转换率达到77.35%。能量分析显示,输入系统的7 468.11 kW能量中,有279.99 kW用于气化供能,4 362.52 kW转化为氢能,系统的能量转换效率为58.42%。经济分析表明,SSEG系统的总资本投资为9.2×108元,是同规模煤制氢工艺的1.2倍,最终氢气成本为18.2元/kg。环境分析结果显示,SSEG−SR工艺处理1 t生物质的全球升温潜能值(GWP)与酸化潜能值(AP)分别为1 036.83 kg和6.40 kg。SSEG−SR工艺的开发与应用,对推动生物质能高效、低碳转化技术向绿氢产业的推广具有重要意义,有助于加速“双碳”目标下的可持续能源转型。

       

      Abstract: In the context of the “dual carbon” goals, biomass energy, as a key component of renewable energy, is gradually becoming an important technological pathway to achieve carbon neutrality. Self-heating adsorption-enhanced biomass gasification (SSEG), as an emerging gasification technology, demonstrates significant advantages in improving hydrogen production and reducing carbon emissions through the synergistic effect of adsorption and gasification. Therefore, the self-heating adsorption-enhanced biomass gasification coupled with steam reforming (SSEG−SR) process was proposed. The process is modeled and simulated using Aspen Plus software, with thermodynamic modeling of the gasification and reforming processes conducted through a Gibbs reactor. Physical property estimations are performed using the Peng-Robinson cubic equation of state combined with the Boston-Mathias function. A comprehensive analysis of the SSEG−SR process chain is conducted from aspects of material flow, energy flow, economic viability, and environmental impact. The accuracy and reliability of the model construction are verified by comparing the simulation results with existing experimental and industrial operation data. Material flow analysis indicates that the SSEG−SR process consumes 7.63 tons of biomass feedstock to produce 1 ton of hydrogen, with a hydrogen conversion rate of 77.35%. Energy analysis shows that, of the 7 468.11 kW input energy to the system, 279.99 kW is used for gasification energy supply, and 4362.52 kW is converted into hydrogen energy, with an overall system energy conversion efficiency of 58.42%. Economic analysis reveals that the total capital investment for the SSEG system is 9.2×108 Ұ, which is 1.2 times that of a coal-to-hydrogen plant of the same scale, with the final hydrogen cost being 18.2 Ұ/kg. Environmental analysis shows that the global warming potential (GWP) and acidification potential (AP) of the SSEG−SR process are 1 036.83 kg and 6.40 kg, respectively. The development and application of the SSEG−SR process provides theoretical support, playing a significant role in advancing the adoption of efficient, low-carbon biomass conversion technologies within the green hydrogen industry. It accelerates the transition to sustainable energy under the dual carbon goals.

       

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