Finite-Time Thermodynamic Simulation of Circulating Direct Condensation Heat Recovery on Chillers

A time series model is used in this paper to describe the progress of circulating direct condensation heat recovery of the compound condensing process (CCP) which is made of two water cooling condensing processes in series for a centrifugal chiller in the paper. A finite-time thermodynamics method is used to set up the time series simulation model. As a result, an upper bound of recoverable condensation heat for the compound condensing process is obtained which is in good agreement with experimental result. And the result is valuable and useful to optimization design of condensing heat recovery.

Thermodynamic Simulation of CCP in Air-Cooled Heat Pump Unit with HFCs and CO₂Trans-Critical

The exergy analysis and finite time thermodynamic methods had been employed to analyze the compound condensation process (CCP). It was based on the air-cooling heat pump unit. The cooling capacity of the chiller unit is about 1 kW, and the work refrigerant is R22/R407C/R410A/CO2. The MATLAB/SIMULINK software was employed to build the simulation model. The thermodynamic simulation model is significant for the optimization of parameters of the unit, such as condensation and evaporation temperature and mass flow of the sanitary hot water and size of hot water storage tank. The COP of the CCP of R410A system is about 3% - 5% higher than the CCP of the R22 system, while CCP of the R407C system is a little lower than the CCP of R22 system. And the CCP of CO2 trans-critical system has advantage in the hot supply mode. The simulation method provided a theoretical reference for developing the production of CCP with substitute refrigerant R407C/R410A/CO2.

自然工质CO2在风冷热泵复合冷凝系统中换热特性的时间序列分析

为研究自然工质CO2在风冷热泵复合冷凝系统中的热力学特性,引入有限时间热力学与■分析方法,采用MATLAB/SIMULINK进行仿真,建立了自然工质CO2在风冷热泵复合冷凝系统的时间序列模型,模拟和测试了自然工质CO2在风冷热泵复合冷凝系统中的热力学特性,并与自然工质CO2单制冷系统及原风冷热泵复合冷凝系统的性能做了对比。结果表明:制热水模式下,两个风冷热泵复合冷凝系统的■效率都随用户要求的卫生热水水温温度升高而降低;达到用户需要水温53℃时,自然工质CO2风冷热泵复合冷凝系统卫生热水机组运行约需18 min,而R22风冷热泵复合冷凝系统约为30 min。复合冷凝模式下自然工质CO2风冷热泵系统的COP(coefficient of performance)为4.7左右,比R22风冷热泵系统略高。

氟系替代工质R407C和R410A与R22在复合冷凝系统中的热力学特性对比研究

目前复合冷凝技术已经形成了行业标准,替代制冷剂在复合冷凝系统中的应用特性研究是一种趋势。有限时间热力学方法和分析方法和SIMULINK软件被引入建立氟系替代制冷剂R407C和R410A在复合冷凝系统的仿真模型,其对象为风冷热泵复合冷凝过程。氟系替代制冷剂R407C和R410A在复合冷凝系统中的热力学特性被模拟,并与原R22系统的性能做了对比。结果表明:R410A复合冷凝系统卫生热水水温上升速度比R22系统快,20 min时上升到约60℃,而R407C复合冷凝系统卫生热水上升速度比R22复合冷凝系统慢,约需50 min水温达到47℃左右。系统效率随用户要求的卫生热水水温温度升高而降低。R410A复合冷凝系统比R22复合冷凝系统略高3%～5%,而R407C复合冷凝系统比R22复合冷凝系统略低。