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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的局限性和反馈效应

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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:与固态干燥剂相比,空调系统(LDAC)中的液态干燥剂有时被视为具有优势,因为可以对溶液进行整体冷却,液相和气相之间的传热和传质要优于固态气体系统,并且溶液可以提供更多的解决方案易于存储并用于负载转移。由于吸附单元(除湿器和蓄热器)包含其他组件(例如内部热交换器)和控制策略(例如体积流量控制),因此整个系统会受到内部反馈和限制。只能从最基本的层面上进行有助于系统理解的研究。为了充分理解LDAC系统的工作原理并检测优化潜力,必须确定系统组件与吸附单元内吸附过程之间的反馈效应。本研究旨在研究溶液热交换器质量,溶液与空气质量流量比和再循环比对稳态系统性能的特定反馈影响。效率-NTU方法用于描述吸附塔的特性。 LiCl的特性数据被示例性地应用于计算。用实验数据校准吸附塔的参数。结果表明,附加热交换器显着决定了单个吸附单元的吸附过程效率。关于焓效率,可以根据热交换器的质量来确定最佳的质量流量比。溶液的再循环率决定了内部溶液的条件,因此对工艺有重大影响。这些发现可以更好地理解LDAC系统,并为基于吸附的空调提供更系统的方法。该过程的心理计量学表示法用于简化对基本反馈效果的理解。

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