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Limitations and Feedback Effects in Liquid Desiccant Air Conditioning Systems

机译:液体干燥剂空调系统中的限制和反馈效果

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Liquid desiccants in air conditioning systems (LDAC) sometimes are seen as advantageous compared to solid desiccants as integrated cooling of the solution is possible, heat and mass transfer between liquid and gas phase is better than in solid-gas systems, and the solution can more easily be stored and used for load shifting. As the sorption units (dehumidifier and regenerator) incorporate additional components (e.g. internal heat exchangers) and control strategies (e.g. volume flow control) the overall system is subject to internal feedback and limitations. Studies to foster system understanding are only available on a very basic level. To fully understand the working principle of a LDAC-system and detect optimization potentials, the feedback effects between the system components and the sorption process within the sorption unit have to be identified. This study aims at investigating the specific feedback effects of solution heat exchanger quality, solution to air mass flow ratio, and recirculation ratio on the steady-state system performance. An efficiency-NTU approach is used to describe the characteristics of the sorption column. Property data of LiCl is applied exemplary for the calculations. Parameters of the sorption column are calibrated with experimental data. Results show that the additional heat exchanger significantly determines the sorption process efficiency of a single sorption unit. With respect to enthalpy efficiency an optimum mass flow ratio can be defined in dependence of the heat exchanger quality. The solution recirculation rate determines the internal solution conditions and therefore has a significant influence on the process. The findings allow for a better understanding of LDAC systems and provide a more systematic approach to sorption based air-conditioning. A psychrometric presentation of the process is used to ease the comprehension of the underlying feedback effects.
机译:空调系统(LDAC)中的液体干燥剂有时被视为与固体干燥剂相比的有利,因为溶液的整合冷却是可能的,液体和气相之间的热量和质量转移优于固体气体系统,溶液更好容易存储并用于负载移位。作为吸附单元(除湿器和再生器)包含附加组件(例如,内部热交换器)和控制策略(例如,体积流量控制)整个系统受内部反馈和限制。促进系统理解的研究仅适用于非常基本的水平。为了完全理解LDAC系统的工作原理并检测优化电位,必须识别系统组分和吸附装置内的吸附过程之间的反馈效果。本研究旨在调查溶液热交换器质量,气体质量流量和再循环比对稳态系统性能的特定反馈效果。效率-NTU方法用于描述吸附柱的特性。应用程序的属性数据是计算的示例。吸附柱的参数用实验数据校准。结果表明,额外的热交换器显着决定了单个吸附装置的吸附过程效率。关于焓效率,可以根据热交换器质量来限定最佳质量流量比。溶液再循环率决定了内部解决方案条件,因此对该过程产生了重大影响。该研究结果允许更好地理解LDAC系统,并提供更系统的基于吸附的空调方法。该过程的心理仪表呈现用于缓解潜在反馈效果的理解。

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