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CFD Modeling of the Multipurpose Hydrogen Test Bed (MHTB) Self-Pressurization and Spray Bar Mixing: Experiments in Normal Gravity: Effect of the Accommodation Coefficient on the Tank Pressure

机译:多功能氢气测试台(MHTB)自加压和喷杆混合的CFD建模:法向重力实验:调节系数对储罐压力的影响

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A CFD model for simulating the self-pressurization of a large scale liquid hydrogen storage tank is utilized in this paper to model the MHTB self-pressurization experiment The kinetics-based Schrage equation is used to account for the evaporative and condensing interfacial mass flows in this model. The effect of the accommodation coefficient for calculating the interfacial mass transfer rate on the tank pressure during tank self-pressurization is studied. The values of the accommodation coefficient which were considered in this study vary from 1.0e-3 to 1.0e-1 for the explicit VOF model and from 1.0e-4 to 1.0e-3 for the implicit VOF model. The ullage pressure evolutions are compared against experimental data. A CFD model for controlling pressure in cryogenic storage tanks by spraying cold liquid into the ullage is also presented. The Euler-Lagrange approach is utilized for tracking the spray droplets and for modeling the interaction between the droplets and the continuous phase (ullage). The spray model is coupled with the VOF model by performing particle tracking in the ullage, removing particles from the ullage when they reach the interface, and then adding their contributions to the liquid. Droplet-ullage heat and mass transfer are modeled. The flow, temperature, and interfacial mass flux, as well as droplets trajectories, size distribution and temperatures predicted by the model are presented. The ullage pressure and vapor temperature evolutions are compared with experimental data obtained from the MHTB spray bar mixing experiment The effect of the accommodation coefficient for calculating the interfacial and droplet mass transfer rates on the tank pressure during mixing of the vapor using spray is studied. The values used for the accommodation coefficient at the interface vary from 1.0e-5 to 1.0e-2. The droplet accommodation coefficient values vary from 2.0e-6 to 1.0e-4.
机译:本文使用一个CFD模型来模拟大型液氢储罐的自加压,以对MHTB自加压实验进行建模。基于动力学的Schrage方程用于解决该界面中的蒸发和冷凝界面质量流。模型。研究了储罐自升压过程中调节界面传质速率对储罐系数的影响。在本研究中考虑的调节系数的值,对于显式VOF模型,从1.0e-3到1.0e-1,对于隐式VOF模型,从1.0e-4到1.0e-3。将空压力变化与实验数据进行比较。还提出了一种CFD模型,该模型通过将冷液体喷入料桶来控制低温储罐中的压力。 Euler-Lagrange方法用于跟踪喷雾液滴并为液滴与连续相(损耗)之间的相互作用建模。喷雾模型与VOF模型耦合在一起,方法是在填充料中执行粒子跟踪,在填充料到达界面时从填充料中除去颗粒,然后将其添加到液体中。对液滴余量的传热和传质进行了建模。给出了模型预测的流量,温度和界面质量通量,以及液滴轨迹,尺寸分布和温度。将空压和蒸气温度的变化与从MHTB喷杆混合实验获得的实验数据进行了比较。研究了在使用喷雾混合蒸气期间,用于计算界面和液滴传质速率的调节系数对罐内压力的影响。界面上用于调节系数的值从1.0e-5到1.0e-2。液滴容纳系数值从2.0e-6到1.0e-4不等。

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