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Fluid dynamics simulations for an open-sorption heat storage drum reactor based on thermophysical kinetics and experimental observations

机译:基于热物理动力学和实验观察的开放吸附式储热鼓式反应器的流体动力学模拟

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摘要

To gain insight into the involved thermodynamic processes of open sorption systems and aid in layout and development of future designs, two different methodologies are presented for the numerical description of adsorption reactors using moving beds. In accordance to earlier laboratory measurements, the molecular sieve Kostrolith 4AK was selected as sorption material and thermo-physical measurements using thermogravimetry with simultaneous differential scanning calorimetry were presented to extract the necessary interpolation functions for modelling the kinetic behaviour. Using discrete particle models in a Navier Stokes CFD Solver and particle simulations based on LIGGGHTS, the mixing characteristics of. the rotating drum setup were accessed. Adsorption based on the thermophysical measurements was implemented into the discrete particle model. Finally, a parametric study with different temperatures and water content in the inflow air was performed using a transient porous volume approach based on the adsorption implementation and different mixing algorithms. Whereas in a simple adsorption kinetic implementation, the volume averaged temperature of the reactor was already significantly reduced after 1.5 h, more realistic implementations showed a prolonged reaction time with a temperature peak at around 15 min. The temperature gap between the temperature of the particles and the usable temperature level for the energy extraction was reduced by introducing a mixing algorithm. In the simulations, zeolite temperature yields could be reached between 15 K and 28 K, corresponding to air temperatures above the material between 21 K and 33 K, which compared well to the experimental observations, where temperature shifts of the process air of up to 36 K were reported. The presented simulation methodology is able to identify partly unused areas in reactors. Numerical optimisation of the flow field and enhancing the particle mixing lead to improved reactor solutions. (C) 2016 Elsevier Ltd. All rights reserved.
机译:为了深入了解开放式吸附系统所涉及的热力学过程,并帮助设计和开发未来的设计,提出了两种不同的方法,用于对使用移动床的吸附反应器进行数值描述。根据较早的实验室测量结果,选择了分子筛Kostrolith 4AK作为吸附材料,并提出了使用热重分析和同时差示扫描量热法的热物理测量方法,以提取必要的内插函数来模拟动力学行为。使用Navier Stokes CFD解算器中的离散粒子模型和基于LIGGGHTS的粒子模拟,实现混合特性。进入旋转鼓设置。基于热物理测量的吸附被实现到离散颗粒模型中。最后,基于吸附方式和不同的混合算法,采用瞬态多孔体积法对流入空气中的温度和含水量进行了参数研究。在简单的吸附动力学实施方案中,反应器的体积平均温度在1.5 h后已经显着降低,而更实际的实施方案显示反应时间延长,温度峰值在15分钟左右。通过引入混合算法,减小了颗粒温度与能量提取可用温度水平之间的温差。在模拟中,沸石的温度屈服可以达到15 K至28 K,这对应于材料上方的空气温度在21 K与33 K之间,这与实验观察结果相吻合,在实验观察中,过程空气的温度变化高达36报告了K。提出的模拟方法能够识别反应堆中部分未使用的区域。流场的数值优化和增强颗粒混合导致改进的反应器解决方案。 (C)2016 Elsevier Ltd.保留所有权利。

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