共查询到19条相似文献,搜索用时 46 毫秒
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根据江南大学体育馆工程设计,气候特点,使用要求,冷热负荷,水源条件,地表水源热泵系统对水温、水质和水量的要求等,进行了地表水源热泵系统的应用设计.详细介绍了水源热泵水系统、机房、自动控制等方面设计情况.阐述了系统设计中的技术要点. 相似文献
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在以往的地表水源热泵设计中,忽略了地表水体的温升可能造成的热污染隐患。作者建议制定专门的地表水体温升范围标准,在工程设计时应计算实际水体可能的温升范围,通过提供足够的冷源水体容积来消除热污染隐患。 相似文献
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结合实际工程,阐明了地表水源热泵系统的节能原理,分析了系统在实际运行过程中的节能特性、经济效益和环境效益,表明该系统具有明显的节能效果、经济效益和环境效益,有一定的推广和应用价值。 相似文献
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指出在地表水源热泵运行中,会因设计不当导致地表水温的升高而造成热污染危害,破坏地表水体的生态环境。因此在进行可行性研究或方案设计时,应根据地表水的水体条件对水体温升情况进行计算预测,采取相关措施消除热污染隐患。 相似文献
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地表水源热泵系统节能系数及环境影响研究 总被引:1,自引:0,他引:1
根据供暖空调的能耗过程,给出节能系数与用能系数的定义,基于热泵系统的运行模式,推导了制热或制冷工况的计算公式。还分析了以大气为冷源的空调系统产生城市热岛效应后的能耗附加值。按现有水源热泵运行性能给出了用能与节能系数定量值,计算了单位水量、单位温变的节能与环保效益。研究表明:地表水源热泵系统节能系数在0.37~1.00之间,热岛效应后的能耗附加值达20%,1.0m3地表水温变1℃节能量达1.55~4.18MJ/ (m3·℃),减少二氧化碳排放达(1.4~2.03)×10-3kg/(m3·℃)。 相似文献
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本文介绍了管式换热法的原理及其优点,基于流动与换热准则关联式,分析比较了套管换热装置的换热特性、阻力特性;利用传热单元数ε-NTU法研究探讨了套管顺、逆两种形式的换热效率,并进一步分析了管式换热法的经济性。研究表明,管式换热法适宜长距离水源条件,应用范围广;套管装置换热Re数高,对流换热系数大50%,但流动阻力为普通换热方式的2~3倍;管式换热形式分为逆流与顺流两种,其中逆流较顺流可减少20%的套管换热面积或长度;另外,套管换热装置比普通换热方式需增加60%的换热管耗材量。 相似文献
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水源热泵空调系统与普通的中央空调系统相比,具有节能热回收以及系统简单,安装方便、操作灵活、适应性强等优点。本文简介其系统组成,工作原理设计要点。 相似文献
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Optimizing the design of large-scale ground-coupled heat pump systems using groundwater and heat transport modeling 总被引:2,自引:0,他引:2
In order to predict the long-term performance of large-scale ground-coupled heat pump (GCHP) systems, it is necessary to take into consideration well-to-well interference, especially in the presence of groundwater flow. A mass and heat transport model was developed to simulate the behavior of this type of system in the Akita Plain, northern Japan. The model was used to investigate different operational schemes and to maximize the heat extraction rate from the GCHP system. 相似文献
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In this study heat pump systems having different heat sources were investigated experimentally. Solar‐assisted heat pump (SAHP), ground source heat pump (GSHP) and air source heat pump (ASHP) systems for domestic heating were tested. Additionally, their combination systems, such as solar‐assisted‐ground source heat pump (SAGSHP), solar‐assisted‐air source heat pump (SAASHP) and ground–air source heat pump (GSASHP) were tested. All the heat pump systems were designed and constructed in a test room with 60 m2 floor area in Firat University, Elazig (38.41°N, 39.14°E), Turkey. In evaluating the efficiency of heat pump systems, the most commonly used measure is the energy or the first law efficiency, which is modified to a coefficient of performance for heat pump systems. However, for indicating the possibilities for thermodynamic improvement, inadequate energy analysis and exergy analysis are needed. This study presents an exergetic evaluation of SAHP, GSHP and ASHP and their combination systems. The exergy losses in each of the components of the heat pump systems are determined for average values of experimentally measured parameters. Exergy efficiency in each of the components of the heat pump systems is also determined to assess their performances. The coefficient of performance (COP) of the SAHP, GSHP and ASHP were obtained as 2.95, 2.44 and 2.33, whereas the exergy losses of the refrigerant subsystems were found to be 1.342, 1.705 and 1.942 kW, respectively. The COP of SAGSHP, SAASHP and GSASHP as multiple source heat pump systems were also determined to be 3.36, 2.90 and 2.14, whereas the exergy losses of the refrigerant subsystems were approximately 2.13, 2.996 and 3.113 kW, respectively. In addition, multiple source heat pump systems were compared with single source heat pump systems on the basis of the COP. Exergetic performance coefficient (EPC) is introduced and is applied to the heat pump systems having various heat sources. The results imply that the functional forms of the EPC and first law efficiency are different. Results show that Exloss,total becomes a minimum value when EPC has a maximum value. Copyright © 2008 John Wiley & Sons, Ltd. 相似文献
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Computer simulation of borehole ground heat exchangers for geothermal heat pump systems 总被引:6,自引:0,他引:6
Computer simulation of borehole ground heat exchangers used in geothermal heat pump systems was conducted using three-dimensional implicit finite difference method with rectangular coordinate system. Each borehole was approximated by a square column circumscribed by the borehole radius. Borehole loading profile calculated numerically based on the prescribed borehole temperature profile under quasi-steady state conditions was used to determine the ground temperature and the borehole temperature profile. The two coupled solutions were solved iteratively at each time step. The simulated ground temperature was calibrated using a cylindrical source model by adjusting the grid spacing and adopting a load factor of 1.047 in the difference equation. With constant load applied to a single borehole, neither the borehole temperature nor the borehole loading was constant along the borehole. The ground temperature profiles were not similar at different distances from the borehole. This meant that a single finite difference scheme was not sufficient to estimate the performance of a borefield by superposition. The entire borefield should be discretized simultaneously. Comparison was made between the present method and the finite line source model with superposition. The discrepancies between the results from the two methods increased with the scale of borefield. The introduction of time schedule revealed a discrepancy between the load applied to the ground heat exchanger and that transferred from the borehole to the ground, which was usually assumed to be the same when using analytical models. Hence, in designing a large borefield, the present method should give more precise results in dynamic simulation. 相似文献
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Among the gas-solid adsorption processes the zeolite water adsorption seems to be very interesting for use in thermodynamic systems such as chemical heat pump, heat transformer and cooling systems. This work evaluates theoretically the best type of zeolite for use in each system on the basis of the adsorption data of zeolites using prefixed operative conditions. Results obtained indicate that thermodynamically a given zeolite type achieves better results than the others for each of the abovementioned systems. Methodology and criterion of comparison used can be applied to other gas-solid processes aiming at realizing chemical heat pump, heat transformer and cooling systems. 相似文献
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