转轮除湿空调系统已经被证实是新型节能环保型空调系统，在可再生能源利用和碳排放方面的优势被广泛认可。传统转轮除湿空调系统是开式系统，高温高湿的再生排风被直接排放在大气中，不仅会造成能源浪费，而且会影响城市热环境，加剧城市热岛效应和温室效应。因此，为了解决传统开式转轮除湿空调系统再生排风能量浪费的问题，提出了太阳能及热泵型闭式转轮除湿空调系统，旨在高效回收和利用再生排风空气的显热和潜热，同时提高开式转轮除湿空调系统的性能。

将能量平衡方程和㶲平衡方程应用于系统的热力学研究，对提出的闭式转轮除湿空调系统和开式转轮除湿空调系统进行了热力学分析，结果表明：闭式转轮除湿空调系统的㶲效率为61.42%，㶲损失为1.025 kW，相比开式转轮除湿空调系统的㶲效率提高了4.08%，㶲损失降低了7.16%。表明提出的闭式转轮除湿空调系统可以显著提高系统的㶲效率，系统热力完善度更高。

设计并搭建了闭式转轮除湿空调系统实验台，研究了主要运行参数对系统性能的影响，结果表明：系统存在最佳的前表冷器、后表冷器和取水换热器的冷水流量比为1:5:4，此时系统的热力性能系数COP_th和㶲效率η最大，分别为1.1和0.501。再生温度对系统性影响较大，当再生温度升高时，COP_th和η显著降低。实际应用中，在满足湿度要求下应尽量降低再生温度并考虑使用可再生热源。在相同运行条件下，改变再生温度从70 ℃增加到120 ℃，提出的闭式转轮除湿空调系统相比开式转轮除湿空调系统的平均COP_th和η分别提高了19.2%和7.7%。

利用TRNSYS模拟软件对太阳能闭式转轮除湿空调系统进行建模，搭建了实验装置验证了模拟的准确性。通过模拟研究了系统的动态性能，结果表明：系统在广州地区整个制冷季的平均电力性能系数COP_e为2.4，平均热力性能系数COP_th为2.1，累计取水量为25657.5 kg，累计热回收量为9696.4 kW。相比太阳能开式转轮除湿空调系统，太阳能闭式转轮除湿空调系统的平均COP_e和COP_th分别提高了42.1%和69.2%，二氧化碳排放量减少了29.3%。

构建了热泵型闭式转轮除湿空调系统。通过对中高温热泵工质的筛选和理论计算，选择了环保工质R1234ze(E)作为系统的循环工质。利用AME sim仿真软件建立了热泵子系统的仿真模型。研究了典型工况下关键耦合参数对热泵子系统性能的影响，结果表明：除湿转轮再生侧空气流量对热泵子系统性能影响较大，除湿转轮再生侧空气流量从0.03 kg/s增加到0.18 kg/s时，冷凝器出口空气温度由98.2 ℃下降到67.1 ℃，COP由3.1升高到3.9；环境空气温度为28 ℃~38 ℃时，热泵子系统表现出良好的热力性能，COP为3.5~4.0，冷凝器出口空气温度可以达到76.6 ℃~85.1 ℃；除湿转轮的处理侧空气流量从0.21 kg/s升高到0.33 kg/s，冷凝器出口空气温度从82.7 ℃升高到86.4 ℃，后蒸发器出口空气温度从17.4 ℃升高到20.6 ℃；除湿转轮处理侧出口空气温度从26 ℃升高到34 ℃，后蒸发器出口空气温度从17.1 ℃升高到20.9 ℃。热泵型闭式转轮除湿空调系统的再生温度和送风温度均满足要求，并且热泵子系统表现出良好的热力性能。

The wheel desiccant air conditioning system has been proved to be a new type of energy saving and environmentally friendly air conditioning system, and its advantages in renewable energy utilization and carbon emissions are widely recognized. The traditional wheel desiccant air conditioning system is an open system. The high temperature and high humidity regenerative exhaust air is directly discharged into the atmosphere, which will not only cause energy waste, but also affect the urban thermal environment and aggravate the heat island effect and greenhouse effect. Therefore, in order to solve the problem of waste of regenerative exhaust energy in the traditional open wheel desiccant air conditioning system, a solar and heat pump closed wheel desiccant air conditioning system is proposed to efficiently recover and utilize the sensible heat and latent heat of the regenerative exhaust air, and improve the performance of the open wheel desiccant air conditioning system.

The energy and exergy balance equations are applied to the thermodynamic study of the system, and the thermodynamic analysis of the proposed closed wheel desiccant air conditioning system is carried out. The results show that the exergy efficiency of the system is 61.42%, and the exergy loss is 1.025 kW. Compared with the traditional open wheel desiccant air conditioning system, the exergy efficiency is increased by 4.08%, and the exergy loss is reduced by 7.16%. It shows that the proposed closed wheel desiccant air conditioning system can significantly improve the exergy efficiency of the system, and the thermal perfection of the system is higher.

The experimental platform of the closed wheel desiccant air conditioning system was designed and built. The influence of the main operating parameters on the performance of the system was studied, and the main conclusions are as follows: the system has the best cold water flow ratio of front surface cooler, rear surface cooler and water intake heat exchanger is 1:5:4, and the COP_th and η of the system are the largest, 1.1 and 0.501, respectively. The regeneration temperature has a significant effect on the system performance, when the regeneration temperature increases, COP_th and η decrease significantly. In practical application, the regeneration temperature should be reduced as much as possible while meeting the humidity requirements, and the renewable heat sources should be fully considered. Under the same operating conditions, changing the regeneration temperature from 70 ℃ to 120 ℃, the average COP_th and η of the proposed closed wheel desiccant air conditioning system increased by 19.2 % and 7.7 %, respectively, compared with the open wheel desiccant air conditioning system.

The TRNSYS simulation software was used to model the solar closed wheel desiccant air conditioning system, and an experimental device was built to verify the accuracy of the simulation. The dynamic performance of the system was studied through simulation, and the results show that during the entire cooling season in Guangzhou, China, the average power COP_e is 2.4, the average thermal COP_th is 2.1, the cumulative water intake is 25657.5 kg, and the cumulative heat recovery is 9696.4 kW. Compared with the solar open wheel desiccant air conditioning system, the average COP_e and COP_th of the solar closed wheel desiccant air conditioning system increased by 42.1% and 69.2%, respectively, and the carbon dioxide emissions decreased by 29.3%.

A heat pump type closed wheel desiccant air conditioning system is constructed. Through the screening and calculation of the working fluid of the medium and high temperature heat pump, the environmentally friendly working fluid R1234ze(E) was selected as the circulating working fluid of the system. The influence of key coupling parameters on the performance of the heat pump subsystem under typical working conditions is studied. The results show that the air flow rate on the regeneration side of the wheel desiccanthas a great influence on the performance of the heat pump subsystem, when the air flow rate increases from 0.03 kg/s to 0.18 kg/s, the air temperature at the outlet of the condenser decreases from 98.2 ℃ to 67.1 ℃, and the COP increases from 3.1 to 3.9. When the ambient air temperature is 28 ℃~38 ℃, the heat pump subsystem shows good thermal performance, the COP is 3.5~4.0, and the outlet air temperature of the condenser can reach 76.6 ℃~85.1 ℃. The air flow rate on the treatment side of the wheel desiccant increases from 0.21 kg/s to 0.33 kg/s, the air temperature at the outlet of the condenser increases from 82.7 ℃ to 86.4 ℃, and the air temperature at the outlet of the rear evaporator increases from 17.4 ℃ to 20.6 ℃. The outlet air temperature of the treatment side of the wheel desiccant increased from 26 ℃ to 34 ℃, and the outlet air temperature of the rear evaporator increased from 17.1 ℃ to 20.9 ℃. The regeneration temperature and air supply temperature of the heat pump type closed wheel desiccant air conditioning system meet the requirements, and the heat pump subsystem shows good thermal performance.

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