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Modeling the dynamic simulation and control of a single effect LiBr-H2O absorption chiller

机译:单效LiBr-H2O吸收式制冷机的动力学仿真与控制建模

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In this study, a dynamic model of a single-effect LiBr-H2O absorption chiller with improved accuracy is built to explore the dynamic performance and the control strategy. Holman correlation is applied to the calculation of heat transfer coefficients of the evaporator, condenser, solution heat exchanger, and generator. The heat and mass transfer in the absorber, chiefly controlled by the mass transfer resistance on the liquid side, are described according to a lumped but accurate physical model based on Nusselt's film theory. The dynamic performance of the absorption chiller is evaluated under the disturbance of the cooling water inlet temperature and heat source temperature. The effect of the thermal mass of the main components on the dynamic performance is explored. Two control strategies are implemented in the model of the absorption chiller: one is setting the chilled water outlet temperature as the manipulated variable, and the other is setting the generator solution temperature as the manipulated variable. The control performances of the two strategies are compared in detail. Results show that either increasing the heat source temperature or decreasing the cooling water inlet temperature increases the risk of crystallization in the dynamic process. The time to reach steady state is highly dependent on the thermal mass of the generator, rather than the thermal masses of the condenser, evaporator, and absorber. The single-effect chiller has better control performance in off-design condition when the generator solution temperature rather than the chilled water outlet temperature is selected as the manipulated variable. (C) 2016 Elsevier Ltd. All rights reserved.
机译:在这项研究中,建立了具有改进精度的单效LiBr-H2O吸收式制冷机的动力学模型,以探索其动态性能和控制策略。霍尔曼相关性用于计算蒸发器,冷凝器,溶液热交换器和发生器的传热系数。根据基于Nusselt薄膜理论的集总但精确的物理模型,描述了吸收器中的传热和传质,主要由液体侧的传质阻力控制。在冷却水入口温度和热源温度受到干扰的情况下评估吸收式制冷机的动态性能。探索了主要部件的热质量对动态性能的影响。在吸收式制冷机的模型中实现了两种控制策略:一种是将冷水出口温度设置为调节变量,另一种是将发电机溶液温度设置为调节变量。详细比较了这两种策略的控制性能。结果表明,提高热源温度或降低冷却水进口温度都会增加动态过程中结晶的风险。达到稳态的时间高度取决于发电机的热质量,而不是冷凝器,蒸发器和吸收器的热质量。当选择发电机溶液温度而不是冷冻水出口温度作为调节变量时,单效冷却器在非设计状态下具有更好的控制性能。 (C)2016 Elsevier Ltd.保留所有权利。

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