翅片式内冷型液体除湿器性能

以氯化锂溶液为除湿剂,建立测试翅片式内冷型液体除湿器性能的试验台,分析溶液和空气进口参数对除湿器性能（除湿量和除湿效率）的影响.     

叉流除湿器传质性能实验研究

除湿器是液体除湿空调系统的核心部件。这里搭建了叉流除湿器性能测试实验台,利用Celdek规整填料作为汽液接触介质,除湿剂选用LiCl-H2O溶液,选取除湿量和除湿效率作为传质性能的评价指标。实验分析了空气、溶液进口参数对传质性能的影响,并利用实验数据建立了适用于LiCl-H2O溶液的叉流除湿效率的实验关联式。最后将实验结果与相关文献中的相关结果进行了比较。发现在实验范围内:与叉流形式相比,逆流除湿器中LiCl-H2O溶液表现出更强的传质性能;在叉流形式的除湿器中,LiCl-H2O溶液的传质性能最优,LiBr-H2O溶液次之,CaCl2--H2O溶液最差。     

溶液除湿空调除湿性能的实验研究

建立了溶液除湿空调除湿性能研究的实验装置,并分别以LiCl溶液、CaCl2溶液及二者等比例的混合溶液为除湿剂,实验研究了空气流量、溶液流量及除湿剂种类对溶液除湿空调除湿性能的影响。     

热泵式溶液除湿新风机组性能研究

溶液除湿是一种具有较大节能潜力的湿度处理方式。本文针对热泵式溶液除湿新风机组进行试验研究,对新送风参数、室内外空气参数、系统功耗等进行测试,分析其除湿能力、制冷能力和能效比。结果表明其除湿效果良好,在与地面辐射系统的共同作用下,室内温湿度达到Ⅱ级热舒适度要求,且除湿性能会随着新风温度或新风含湿量的升高而增强。此外,将新风处理到同样的状态,溶液除湿较冷凝除湿直接节能54.8%,冷冻水温度提高近10℃也间接提高了系统的能效比,溶液除湿节能方面优势明显。     

叉流除湿器热质传递性能实验研究

在太阳能溶液除湿蒸发冷却空调系统实验台上,以LiCl溶液为除湿剂,用空气进出口含湿量差和除湿效率作为除湿过程的性能评价指标,来研究叉流除湿器的除湿性能。通过实验数据分析了溶液、空气进口参数对除湿性能的影响,并利用实验数据建立适用于LiCl溶液的叉流除湿器的除湿效率和传质系数的实验关联式,发现与实验结果的吻合程度很好,误差在15%以内,能够利用这些关联式来准确的计算叉流除湿器的除湿性能,可供叉流除湿器设计参考使用。最后将实验结果与相关文献进行比较,结果表明:不同的除湿剂对叉流除湿器的除湿性能的影响基本相同。     

迷宫精馏型溶液除湿空调机组的试验分析

机组选用自主研发的迷宫精馏型溶液除湿（再生）器,通过改善空气流动方向,增加溶液与空气的接触时间,提高溶液的吸收能力。分别测试机组在名义除湿工况、名义制冷工况和全新风工况下的除湿能力,测试结果表明机组在全新风工况下的除湿能力最好。     

无霜空气源热泵系统除湿与再生工况?分析

为解决传统空气源热泵系统冬季的结霜问题,同时提升夏季机组的性能,本文提出一种"一塔三用"的无霜空气源热泵系统。通过搭建实验台研究了在除湿工况下的空气温度、含湿量、质量流量及溶液温度、质量流量、质量浓度,在再生工况下的溶液质量浓度、温度对溶液塔进出口空气?、除湿?(再生?)、系统输入输出?及?效的影响。结果表明:除湿工况下,除湿?随空气温度、空气质量流量、溶液质量流量的增加以及空气含湿量、溶液温度、溶液质量浓度的减少而增加;系统的?效随空气温度、含湿量、质量流量及溶液质量流量、质量浓度的增加以及溶液温度的减少而增加,其中空气含湿量、溶液质量浓度对?效影响较小,此模式?效最高可达0. 201。再生工况下,再生?随溶液质量浓度、温度的增加而增加;系统?效随溶液质量浓度的增加、溶液温度的减少而增加,其中溶液温度对?效影响较小,此模式?效最高可达0. 108 8。该系统?效率在实验工况下高于常规空气源热泵系统。     

无霜空气源热泵系统喷淋溶液质量及浓度变化规律研究

本文提出了无霜空气源热泵系统及其工作过程,根据提出的无霜空气源热泵的原理,进行了喷淋溶液的筛选。分析目前常用的除湿溶液,主要从蒸汽压力、凝固点、粘度、经济性等方面对常用的有机除湿溶液进行比较,最后确定丙三醇（甘油）作为室外换热器的喷淋溶液。通过比较不同溶液浓度和流量对除湿性能及机组性能的影响来找到合理的喷淋溶液的浓度和喷淋溶液的流量。然后使用这个浓度和流量在不同的室外气候条件下向室外换热器喷淋除湿溶液,分析不同室外条件对除湿效果和抑制结霜效果的影响,整理出室外风机风量、室内供热量、输入功率、COP、喷淋溶液截留的水量等参数的变化。最后通过实验数据分析喷淋溶液集中再生的条件,分析不同地区喷淋溶液集中再生的可行性及不同地区集中再生需要的稀溶液罐和浓溶液罐体积,为无霜空气源热泵的应用提供参考。     

液体除湿空调除湿器性能研究

在液体除湿空调中,除湿器是系统的核心部件。本文搭建可用于实验研究的液体除湿空调系统中除湿器的实验台,对塔径300 mm、填料高度800 mm,以Li Cl溶液为除湿剂的除湿器布置测点进行实测。基于Mercel理论,根据热质平衡并结合D.I.Stevens的有效模型,建立适用于该液体除湿空调系统中的除湿器传热传质模型。从实验和理论模型两个方面分析除湿器进口各项参数对除湿量的影响,结果表明:理论值和实验值有很好的一致性,且数据差异较小,说明计算模型适应性良好,能准确的用于该除湿器的性能模拟测试,将实验与理论计算结果进行对比可知:在一定的工况范围内,除湿器的除湿量受进口溶液温度、浓度、质流密度等参数影响较大,其中溶液进口温度越低,除湿效果越显著,溶液进口浓度越低,除湿效果越好;溶液进口质流密度需控制在一定范围进行调节,才能显著提高除湿器性能;空气入口风速、干球温度以及含湿量对除湿出口的空气状态参数影响较弱。     

除湿溶液蒸汽压的研究

除湿溶液表面蒸汽压的大小直接影响液体除湿空调系统的性能,在常用的除湿剂中由于氯化钙的价格低廉,是一种比较经济的除湿剂,但它的缺点是蒸气压比较高,除湿效果不稳定,而氯化锂的价格高,水蒸气压较低且稳定,是一种性能非常优良的除湿剂.为了提高除湿溶液的除湿性能和降低其价格,可以把两种除湿剂按不同的比例进行混合,就可以得到性价比比较好的除湿溶液.文中应用经典热力学理论研究了常用除湿溶液表面蒸汽压的形成机理.对氯化钙、氯化锂及其混合溶液表面蒸汽压进行了计算,计算结果和实验结果非常接近,认为该方法可以用来较准确的估算各类除湿溶液的蒸汽压,为液体除湿空调系统中除湿剂的选择提供理论依据.     

机械蒸气再压缩系统再生高浓度溶液的性能研究

机械蒸气再压缩(MVR)系统是一种高效的蒸发系统,本文通过模拟与实验的方法对MVR系统再生高浓度CaCl2溶液的性能进行研究,分析了蒸发压力、入口溶液质量浓度等输入参数对MVR系统再生性能的影响.研究结果表明:蒸发压力通过吸气密度影响再生速率,蒸发压力越大,再生速率越大,系统能耗越大;入口CaCl2溶液质量浓度为0.3...     

The investigation of parameters affecting boron removal by electrocoagulation method

Boron removal from wastewaters by electrocoagulation using aluminum electrode material was investigated in this paper. Several working parameters, such as pH, current density, boron concentration and type and concentration of supporting electrolyte were studied in an attempt to achieve a higher removal capacity. The experiments were carried out by keeping the pH of solution constant and optimum pH of solution was determined 8.0 for the aluminum electrode. Although energy consumption increased with decreasing boron concentration, which conductivity of these solutions were low, boron removal efficiency was higher at 100 mg/L than that of 1000 mg/L. Current density was an important parameter affecting removal efficiency. Boron removal efficiency and energy consumption increased with increasing current density from 1.2 to 6.0 mA/cm2. The types of different supporting electrolyte were experimented in order to investigate to this parameter effect on boron removal. The highest boron removal efficiency, 97%, was found by CaCl2. Added CaCl2 increased more the conductivity of solution according to other supporting electrolytes, but decreased energy consumption. The results showed to have a high effectiveness of the electrocoagulation method in removing boron from aqueous solutions.     

新型电动汽车热泵系统除湿再热性能实验研究

本文设计了一种具备两种除湿再热模式的电动汽车热泵系统,在不同实验工况下研究了两种除湿再热模式的除湿性能与再热性能。结果表明:热泵系统的功耗低于2.0 kW,COP大于2.0;除湿再热模式A的除湿率为0.41～0.83 kg/h,制热量为1.7～3.0 kW;除湿再热模式B的除湿率为0.25～0.55 kg/h,制热量为2.0～3.4 kW。因此除湿再热模式A具备良好的除湿性能,除湿模式B具备良好的再热性能;根据两种除湿再热模式的特点,提出了一种既能满足乘员舱除湿供暖要求,又相对节能的运行策略。     

Investigation on capacity matching in a heat pump and hollow fiber membrane-based two-stage liquid desiccant hybrid air dehumidification system

The heat pump and hollow fiber membrane-based two-stage liquid desiccant hybrid air dehumidification system is promising recently because solution droplets can be prevented from crossing over into the process air. The quasi-isothermal processes are realized by two-stage dehumidification processes and the system performance is improved. In this study, a novel capacity matching index (CMI) is introduced to evaluate the energy capacity matching of the system through modeling study. It is found that CMI is usually lower than 1 under the typical hot and humid weather condition like South China and the demand and supply of energy in the system is mismatching. As inlet air temperature rises, the dehumidification rates, CMI, EER and COP all decrease. But CMI is almost constant with different inlet air humidity. The influence of air inlet temperature to dehumidifiers and regenerators on the system performance is also investigated. The higher the inlet temperature of dehumidifiers is, the larger the CMI, EER and COP are. The dehumidification rates and CMI both grow with an increase in the inlet temperature of regenerators. It is beneficial for energy balance of the system and high moisture loads, but the side effect is that the EER and COP both decrease.     

涂覆MIL-101(Cr)干燥剂的翅片管换热器的实验研究

干燥剂涂层换热器(DCHE)是一种新开发的翅片管表面带有干燥剂涂层的换热器,它可以同时处理潜热和显热.为了获得更高的性能,高孔隙度的金属有机框架(MOF)被引入到设计中.本文通过水浴法成功合成MIL-101(Cr)材料,并对材料进行X射线衍射(XRD)、N2吸附-脱附测试、水蒸气吸脱附曲线、电镜扫描等系列物理表征.制作...     

凹土-氯化钙复合吸附剂的制冷性能

采用凹凸棒粘土和氯化钙为主要原料,用溶解-混合法制备了复合吸附剂;采用正压重量法测量了复合吸附剂对氨的吸附等温线;并测定了吸附剂-氨工质对的制冷特性。结果表明:吸附温度30℃下,复合吸附剂对氨的平衡吸附量为1.1kg/kg,与氯化钙对氨的平衡吸附量相当。在装填密度为600kg/m3,吸附温度为30℃、蒸发压力为0.25MPa、解吸温度为300℃条件下,对氨的吸附量达到0.89~0.92kg/kg,循环吸附量为0.55~0.58kg/kg,是纯氯化钙的1.7倍;复合吸附剂-氨工质对制冷量可达761.84kJ/kg,比氯化钙-氨工质对提高了70%。而且,复合吸附剂具有良好的吸附解吸稳定性能。     

Investigation on capacity matching in liquid desiccant and heat pump hybrid air-conditioning systems

Liquid desiccant and heat pump (LDHP) hybrid air-conditioning system provides a promising independent air dehumidification solution. Capacity matching among the four major heat and mass transfer components, i.e. dehumidifier, regenerator, evaporator and condenser, is essentially important for energy efficiency of the hybrid system. In this paper, the configuration of the hybrid system is firstly studied. Novel matching indices are proposed to evaluate the matching effect. The results show that a LDHP hybrid system with double-condenser, one solution-cooled and one air-cooled, is a feasible configuration for achieving capacity matching. To achieve dynamic capacity matching under real changing operating conditions, the effects of three critical operating variables, including solution flow rate, revolution of the compressor and air flow rate in the air-cooled condenser, on capacity matching and energy performance are studied. Simulation results show that dynamic capacity matching can only be achieved by regulating these three operating variables simultaneously.     

Cycle analysis of an air-cooled LiBr/H2O absorption heat pump of parallel-flow type

A gas-fired absorption heat pump with cooling capacity of 2 RT was analysed as an air-conditioner for domestic use during the summer. The absorption heat pump considered was an air-cooled, double-effect, LiBr/H₂O system of parallel-flow type. The performance of the absorption heat pump in the cooling mode of operation was investigated through cycle simulation to obtain the system characteristics depending on the inlet temperature of air to the absorber, the working solution concentrations, the solution distribution ratio of the mass of solution into the first generator to the total mass of solution from the absorber, and the LTDs (leaving temperature differences) of the heat-exchanging components. When the predicted results were compared with the measured data for similar design conditions, reasonable agreement was observed. The optimum design and operating conditions of an air-cooled absorption system are suggested based on this cycle simulation analysis.     

离子改性的聚丙烯酸除湿换热器系统性能研究

干燥剂吸附性能对除湿换热器系统的除湿性能有重要影响。本文通过改进的ASAP2020气体吸附仪和恒温恒湿箱,先后对Na+和K+改性的聚丙烯酸聚合物的水蒸气平衡吸附性能和吸附动力学特性进行了测试研究,并与硅胶相对比。研究结果表明:平衡吸附测试显示Na⁺改性的聚丙烯酸在整个相对压力区间性能优于硅胶,K⁺改性的在高相对压力区间(>0. 8)逊于硅胶;基于Polanyi吸附势理论对干燥剂吸附特征曲线进行拟合,以用于后续的除湿换热器模拟研究;动态吸附性能表明聚丙烯酸干燥剂的吸附速率均低于硅胶,但Na⁺改性的聚丙烯酸整个吸附过程的动态吸附量仍多于硅胶;通过模拟除湿换热器除湿性能,在ARI summer、ARI humid和上海夏季这3种典型室外工况下,Na⁺改性的聚丙烯酸换热器可以从待处理空气中去除更多的水分,较硅胶换热器提升49%～118%,适用于室外湿度较小的气候工况。     

Experimental study on silica gel-LiCl composite desiccants for desiccant coated heat exchanger

Desiccant coated aluminum-fin is an important part in desiccant coated heat exchanger (DCHE). It will affect the overall performance of this novel solid desiccant component. In the paper, different silica gel-LiCl composite desiccant coated aluminum sheets were fabricated and some key parameters were studied. Nitrogen adsorption suggested that texture properties of composite desiccants were different from silica gel due to impregnated salt and combined action of silica sol and silica gel. The highest thermal conductivity of composite sheets was 5.8 Wm⁻¹K⁻¹, which is twice of silica gel coated one. Sorption kinetics indicated that composite sheets exhibited higher dynamic sorption quantities and faster sorption rates. Sorption isotherms were also obtained and fitted with Dubinin–Astakhov equation. Besides, dehumidification capacity of composite DCHE was tested and compared with silica gel one. Results indicated that enhanced dehumidification capacity can be achieved with use of composite desiccant in the DCHE system.