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翅片管束储氢反应器反应死区优化的数值模拟

Numerical Simulation of Reaction Dead Zone Optimization for Finned Tube Bundle Hydrogen Storage Reactor

  • 摘要:
    目的 金属氢化物导热系数低且储氢过程存在强烈的放热效应,导致反应速率下降,文章聚焦储氢反应器的热管理问题,研究反应器几何参数对储氢性能的影响。
    方法 通过建立翅片管束储氢反应器的二维数值计算模型,研究反应器半径、壁厚对储氢速率和反应死区的影响,获得不同半径下较优的反应器壁厚,并据此进行变工况研究,得到优化的储氢条件。
    结果 结果表明:随反应器壁厚增加,储氢速率逐渐增大,床层边缘反应死区不断缩小,反应器半径为25 mm时,存在较优的壁厚5 mm使储氢时间接近300.0 s;当反应器半径为35~55 mm时,较优的壁厚分别为10 mm、15 mm和15 mm,三者的储氢时间变化幅度小于1.69%,但半径大于55 mm时,不宜通过增加壁厚优化反应死区。此外,优化的储氢条件为储氢压力1.2 MPa、换热流体温度283.15 K和对流换热系数2500 W/(m2·K),相较优化前储氢时间缩短了39.44%。
    结论 壁厚优化可有效消除不同半径翅片管束反应器的反应死区,该研究成果可为金属氢化物储氢反应器的工程应用提供指导。

     

    Abstract:
    Objective Metal hydrides suffer from low thermal conductivity, and their highly exothermic hydrogen storage process impedes reaction kinetics. This paper focuses on the thermal management of hydrogen storage reactors, investigating the impact of geometric parameters on storage performance.
    Method By developing a two-dimensional numerical model of a finned tube bundle hydrogen storage reactor, this study investigated the effects of reactor radius and wall thickness on the hydrogen absorption rate and the formation of reaction dead zones. Optimal wall thicknesses were determined for various reactor radius, which then served as the basis for a parametric study to identify optimized hydrogen storage conditions.
    Result The results indicate that increasing the reactor wall thickness enhances the hydrogen absorption rate and shrinks the reaction dead zones near the bed periphery. For a reactor with a 25 mm radius, an optimal wall thickness of 5 mm yields a near-minimum absorption time of approximately 300.0 s. For radius of 35~55 mm, the optimal thicknesses are 10 mm, 15 mm, and 15 mm, respectively, with the corresponding absorption times varying by less than 1.69%. However, for radius exceeding 55 mm, further increasing the wall thickness is no longer an effective strategy for optimizing the dead zone. Furthermore, the optimized operating conditions—a storage pressure of 1.2 MPa, a heat transfer fluid temperature of 283.15 K, and a convective heat transfer coefficient of 2500 W/(m2·K)—shortened the absorption time by 39.44% compared to the initial conditions.
    Conclusion Optimizing the reactor wall thickness can effectively eliminate reaction dead zones in finned tube reactors across a range of radius. These findings provide valuable guidance for the engineering design and application of metal hydride hydrogen storage reactors.

     

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