共查询到18条相似文献,搜索用时 140 毫秒
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针对常规转轮除湿空调系统再生能耗高、再生排风热损失大的问题,提出了热泵再生型转轮除湿空调系统,该系统能同时回收转轮除湿侧的吸附热及再生侧的排风热。研究热泵再生型转轮除湿空调系统的热力过程,进而建立该系统的■能耗模型。分析室外气象参数对系统性能的影响,随着室外空气温度的升高,系统的■损耗减少,■效率提高;随着室外空气含湿量的提高,系统的■损耗先减少后增加;当室外干球温度低于34.0℃,含湿量低于20.3 g/kg(相对湿度为59.8%)时,系统的送风参数能满足室内舒适性要求。结果表明热泵再生型转轮除湿空调系统较适用高温中湿的室外环境。 相似文献
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针对常用的转轮除湿空调系统能耗高的问题,通过理论分析,提出了转轮除湿机与预冷器或热回收装置不同组合下的三种节能型转轮除湿空调系统,并建立相应的能耗数学模型。实例能耗分析表明:有预冷的转轮除湿空调系统比无预冷的转轮除湿空调系统总能耗低40.9%~43.8%;有热回收转轮的除湿空调系统比无热回收转轮的除湿空调系统总能耗低16.1%~20.2%;预冷热回收型转轮除湿空调系统能耗最低,比传统冷却除湿空调系统节能12.8%。处理空气先预冷后除湿和增加热回收装置的措施可大大降低转轮除湿空调系统能耗。 相似文献
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针对现有的蒸发冷却系统冷量不足的问题,提出了基于太阳能驱动转轮除湿的蒸发冷却冷水系统。系统由太阳能热水、低温驱动双转轮除湿及露点式蒸发冷却冷水三个子系统组成。太阳能热水系统为低温驱动双转轮除湿系统提供再生驱动热源。低温驱动双转轮除湿系统为露点式蒸发冷却冷水系统提供低露点的处理空气。研究了系统的工作原理、热力学过程,并建立系统的热力计算模型,研究结果表明:在典型夏季实例下,当系统再生温度取80℃时,系统出水温度低至12℃,相比传统直接蒸发冷却系统的理想出水温度25. 8℃,降低了53. 5%,湿球效率可达248. 4%。结果表明基于太阳能驱动转轮除湿的蒸发冷却冷水系统能很好解决传统蒸发冷却系统冷量不足的问题,使该系统替代传统压缩式冷水机组成为可能。 相似文献
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转轮除湿空调系统是将转轮除湿机与常用冷却方式相结合实现空调制冷的新型空调系统。为降低转轮除湿空调系统的再生能耗以及提高系统的冷却能力,本文提出双级热管转轮除湿空调系统,系统利用重力热管的冷凝段实现转轮除湿机的再生,蒸发段实现处理空气的冷却。建立了双级热管除湿转轮空调系统传热传湿模型,模拟分析了系统在不同工况下系统的降温除湿特性。研究表明,处理空气进口温度越高,系统的冷却能力越强但系统的除湿能力降低;处理空气湿度越高,系统的除湿能力越强,但系统的冷却能力降低;再生温度越高,系统除湿能力越强,系统热力性能系数越低,但冷却能力降低。综合降温除湿能力及节能要求,双级热管转轮除湿空调系统的再生温度不宜过高,推荐≤80℃。 相似文献
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范红梅 吴晓蕾 郭俊盛 甘再国 秦芝 雷相国 董成富 徐华根 陈若富 张福明 郭斌 刘洪业 王华磊 谢成营 冯兆庆 郑勇 宋立涛 骆鹏 徐瑚珊 周小红 任中洲 靳根明 《中国物理 C》2005,(5)
主要介绍了合成和鉴别107号元素的新同位素265Bh的实验装置、实验方法以及实验结果.目标核265Bh是由能量为135MeV的26Mg离子轰击243Am靶,通过融合蒸发反应而产生.反应产物首先由He jet系统传输到装有数个探测器对的转轮收集测量系统,然后依靠母子核遗传关系通过观察新同位素和它们已知子核261Db和257Lr之间的α衰变的关联,来实现对新核素的鉴别.实验测得265Bh的α衰变能量为(9.24±0.05)MeV, 半衰期为0.94+0.70-0.31s.从该实验得出的265Bh的α衰变能量和半寿命能够与理论预言一致. 相似文献
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主要介绍了合成和鉴别107号元素的新同位素265Bh的实验装置、实验方法以及实验结果.目标核265Bh是由能量为135MeV的26Mg离子轰击243Am靶,通过融合蒸发反应而产生. 反应产物首先由He-jet系统传输到装有数个探测器对的转轮收集测量系统,然后依靠母子核遗传关系通过观察新同位素和它们已知子核261Db和257Lr之间的a衰变的关联,来实现对新核素的鉴别. 实验测得265Bh的a衰变能量为(9.24±0.05)MeV, 半衰期为0.94+0.70 -0.31s. 从该实验得出的265Bh的a衰变能量和半寿命能够与理论预言一致. 相似文献
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《Heat Recovery Systems and CHP》1991,11(6):563-572
This communication presents some studies on hybrid vapor-compression (V-C) and solid/liquid desiccant solar air-conditioning systems. Desiccants are used to bring the humidity within the comfort range by partially converting the latent heat load (LHL) into sensible heat load and then meeting this load with conventional V-C cycle. In both the options of hybrid systems consisting of vapor-compression and solid/liquid desiccant cycles, heat rejected from the condenser of the V-C cycle is used to regenerate the desiccants to improve the coefficient of performance (COP) of the systems. A thermodynamic assessment and technoeconomic feasibility study of hybrid V-C and solid/liquid desiccant solar air-conditioning systems have been presented. It is found that a hybrid system with desiccant cycle is more promising under high latent heat load and higher ambient humidity conditions and significant energy saving can be achieved over standard V-C cooling systems. 相似文献
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空气调节过程中,冷凝除湿方式要求制冷剂的蒸发温度低于空气的露点温度,限制了空调器效率的提高.本文在传统的热泵空调机组的基础上,添加一个溶液除湿循环,利用吸湿性溶液调节空气的含湿量,此时制冷剂的蒸发温度可以较大幅度地提高,吸湿后的溶液用冷凝器的排热再生。文章计算了复合式空调机组在两种工作模式下的性能,研究了内部冷却流体温度、回热器效能和室外空气状态等因素对机组性能的影响。分析结果表明,溶液式复合空调机组具有较大的温、湿度调节范围,且机组效率较冷凝除湿机组显著提高。 相似文献
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《Heat Recovery Systems and CHP》1988,8(6):537-548
A mathematical model describing the heat and mass transfer processes that occur during sorption of water vapor in a dehumidifier consisting of parallel channels lined on either side width desiccant felt, is presented. The model includes both gas-side and solid-side resistances for thermal and mass transport. The moisture transport in the desiccant is expressed by considering both gas phase diffusion and surface diffusion. The heat and mass transfer in the desiccant matrix occurs simultaneously and is coupled by an equilibrium sorption relation which is applied locally within the desiccant. Solutions are obtained by using an explicit finite-difference scheme.The effect of heat and mass transfer Biot numbers and other system parameters on the performance of an adiabatic open-cycle cooling system are investigated. 相似文献
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In this paper, an energy and exergy analysis is applied to the air dehumidification unit of a liquid desiccant system in an industrial gelatin conveyor dryer. The working fluid is a binary solution of lithium chloride (LiCl) in water. Dry air is used in order to decrease the amount of liquid in the gelatin. Therefore, the environmental air must have its absolute humidity reduced from about 12 g/kg to the project target, which is 5 g/kg. The process is a cycle using an absorption desiccant unit (LiCl in water), where the weak solution absorbs water vapor from the air. In the regenerator, condensation of the solution (desorption) from the moist air occurs. As a result, the steam consumption of the desorber and electrical power used for the vapor compression chiller (with ammonia, NH, as working fluid) are the primary sources of cost for the factory. To improve the plant’s energy and exergy behaviors, the process is evaluated using a mathematical model of the system processes. In addition, we evaluate the substitution of the vapor compression chiller by an absorption unit (lithium bromide (LiBr) in water). The performance indicators of the compression vapor systems showed the best results. Even when using the condenser’s energy to pre-heat the solution, the installed system proved to be more effective. 相似文献
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Desiccant integrated hybrid vapor-compression cooling: Performance sensitivity to outdoor conditions
《Heat Recovery Systems and CHP》1988,8(6):489-501
The performance of a desiccant integrated, hybrid, vapor-compression cooling system is modeled numerically. The concept of hybrid cooling investigated in this paper utilizes the waste heat rejected from a vapor-compression cycle to directly activate a solid desiccant dehumidification cycle. The hybrid system consists of four major components; a compressor, an evaporator and two desiccant integrated condensers/dehumidifiers. The performance sensitivity of a first generation prototype hybrid, vapor-compression cooling system to variable outdoor conditions is reported and compared to the performance of conventional vapor-compression systems. 相似文献