首页|基于机器学习的CO2催化加氢制航空煤油筒式反应器数学模拟分析与优化

基于机器学习的CO2催化加氢制航空煤油筒式反应器数学模拟分析与优化

扫码查看
借助Fe基催化剂,CO2通过加氢反应可成功转化为高附加值的航空煤油,具有很好的工业应用潜力。目前缺少准确适宜的CO2加氢合成航空煤油的反应器模型,因此亟需对其反应模型进行构建,为相关工艺的工业化提供参考。通过机器学习探究实验条件和关键组分CO和CO2物质的量分数关系,构建了关键组分CO和CO2预测模型;基于Anderson-Schulz-Flory分布规律,构建了碳链增长模型,进一步构建了产物分布模型;基于催化床层物料衡算、热量衡算和压降计算,建立了筒式固定床反应器的一维拟均相模型;通过模拟一定工艺条件得到了CO2加氢合成航空煤油的反应结果,并对工艺条件进行了模拟优化。模拟结果表明,反应器进口温度升高、空速增大,CO2转化率降低,航空煤油集总组分C11H24时空产率增加;操作压力增大,CO2转化率增加,C11H24时空产率在反应压力为2。0 MPa时最高;饱和沸腾水温度升高,CO2转化率和C11H24时空产率增加。最佳CO2加氢制航空煤油反应条件:反应器进口温度为275℃、进口压力为2。0 MPa、空速为4000 h-1和饱和沸腾水温度为294℃。此时CO2转化率为21。95%,C11H24时空产率为12。14 g/(L·h),床层压降为0。20 MPa。
Mathematical simulation analysis and optimization of cylinder reactor for CO2 catalytic hydrogenation to jet fuel based on machine learning
With Fe-based catalyst,CO2 can be successfully converted into high value-added jet fuel via hydrogenation,showing great potential of industrial application.There is a lack of accurate and appropriate reactor model for CO2 hydrogenation to jet fuel,therefore it is urgent to construct reaction model and provide reference for the industrialization of related processes.The relationship between experimental conditions and mole fraction of key components CO and CO2 was explored through machine learning,and the prediction model of the key components CO and CO2 was constructed.Based on the Anderson-Schulz-Flory distribution,the carbon chain growth model was established,and the product distribution model was further constructed.Moreover,based on the calculation results of material balance,heat balance and pressure drop,homogeneous one-dimensional model of cylindrical fixed-bed reactors was established.The results of CO2 hydrogenation to jet fuel were obtained by simulating operation conditions,and the operation conditions were optimized.The simulation results show that CO2 conversion rate decreases and space time yield of jet fuel lumped component C11H24 increases with the increase of inlet temperature and space velocity.CO2 conversion rate increases with the increase of operating pressure.The operating pressure of maximum space time yield of C11H24 is 2.0 MPa.CO2 conversion rate and space time yield of C11H24 increase with temperature of saturated boiling water increasing.The optimum reaction conditions are inlet temperature of 275℃,inlet pressure of 2.0 MPa,space velocity of 4000 h-1 and saturated boiling water temperature of 294℃.Currently,the CO2 conversion rate is 21.95%,the space time yield of C11H24 is 12.14 g/(L·h),and the pressure drop is 0.20 MPa.

CO2 hydrogenationjet fuelmachine learningcylindrical fixed-bed reactorreactor simulation

黄成、刘操、黄磊、崔灵瑞、马宏方、曹发海

展开 >

华东理工大学 化工学院,上海 200237

华东理工大学 化工学院 大型工业反应器工程教育部工程研究中心,上海 200237

CO2加氢 航空煤油 机器学习 筒式固定床反应器 反应器模拟

2024

天然气化工—C1化学与化工
西南化工研究设计院有限公司 全国天然气化工与碳一化工信息中心

天然气化工—C1化学与化工

CSTPCD北大核心
影响因子:0.814
ISSN:1001-9219
年,卷(期):2024.49(7)