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1.
考虑高低温侧换热器、回热器和中冷器的热阻损失,以及压气机和涡轮中的不可逆损失,以功率为优化目标,借助数值计算,研究了恒温热源条件下不可逆闭式中冷回热布雷顿循环输出功率最大时高低温侧换热器、回热器和中冷器的热导率分配以及中间压力与总压比的关系。  相似文献   

2.
考虑高低温侧换热器、回热器和中冷器的热阻损失,以功率为优化目标,对恒温热源条件下内可逆闭式布雷顿循环的高低温侧换热器、回热器和中冷器的热导率以及中间压比的分配进行了优化。借助数值计算,分析了一些主要循环特征参数对最大功率及相应热导率和中间压比分配、双重最大功率的影响。  相似文献   

3.
用有限时间热力学方法优化恒温热源条件下闭式中冷回热燃气轮机循环的生态学性能,计入工质与高低温侧换热器、回热器以及中冷器之间的热阻损失、压气机内不可逆压缩和涡轮内部不可逆膨胀损失,导出了循环生态学函数解析式,通过数值计算优化各换热器热导率分配以及中间压比和总压比,得到了循环最优生态学性能.  相似文献   

4.
变温热源内可逆中冷回热布雷顿循环功率密度优化   总被引:1,自引:0,他引:1  
以功率密度为目标,用有限时间热力学的方法,通过数值计算,对变温热源条件下的内可逆中冷回热布雷顿循环的高、低温侧换热器的热导率分配和中间压比、循环总压比和工质与热源间的热容率匹配进行优化。分别得到了最大功率密度、双重最大功率密度和三重最大功率密度,并分析了热力学参数对高低温侧换热器的热导率最优分配、最佳中间压比、最大功率密度和双重最大功率密度的影响。  相似文献   

5.
计入高低温侧换热器和中冷器的热阻损失、压气机和涡轮机中的不可逆压缩和膨胀损失及管路中压力损失,用有限时间热力学方法导出了变温热源条件下不可逆闭式燃气轮机中冷循环功率和功率密度(功率与循环中最大比容之比)的解析式;分别以功率和功率密度为目标,优化了中间压比、高低温侧换热器及中冷器热导率分配,并对结果进行了比较.  相似文献   

6.
考虑循环过程的内外不可逆性,以生态学函数为目标,优化了总压比和中间压比分配,分析了高低温侧换热器、中冷器和回热器的性能参数对最大生态学函数及其参数的影响,并与以功率为优化目标时的循环性能进行了比较.结果表明:以生态学函数为优化目标时比以功率为优化目标时具有更高的效率,但功率相差不太多,反映了输出功率和效率间的最佳匹配.  相似文献   

7.
采用有限时间热力学的思想,建立了高炉余能余热驱动的变温热源不可逆中冷回热(ICR)布雷顿热电联产(CHP)装置模型.以(火用)输出率和炯效率为目标优化了装置的性能,发现回热器对炯性能的影响在所有换热器中是最小的,当给定回热器热导率分配时,分别存在两个最佳的中间压比和两组最佳的高、低温侧和热用户侧换热器以及中冷器的热导率分配使炯输出率和炯效率取得最大值.进一步优化总压比,得到了双重最大(火用)输出率和炯效率.增大高炉余热源入口温度、压力恢复系数、压气机和涡轮机效率有利于提高装置的炯性能,在一定范围内,热用户温度越高越好.最后发现分别存在最佳的工质与热源间的热容率匹配使(火用)输出率和(火用)效率取得三重最大值.  相似文献   

8.
不可逆中冷回热太阳能布雷顿循环系统的优化分析   总被引:1,自引:0,他引:1  
建立了由太阳能集热器模型和不可逆中冷回热布雷顿循环模型组成的恒温热源条件下太阳能布雷顿循环系统,以系统总效率为目标函数,考虑了高低温侧换热器、回热器和中冷器的热阻损失以及压缩机和涡轮机的不可逆损失,借助数值计算对太阳能集热器的工作温度进行了优化,并分析了主要特征参数对总效率的影响.结果表明:太阳能布雷顿循环系统中存在一个最佳的太阳能集热器工作温度和相应的最大总效率及最大总输出功率;在此基础上,通过优化中间压比可使循环系统的总效率和相应的总输出功率达到双重最大值;系统总效率随着回热器传热有效度和光学效率的增加而提高;系统运行时存在一个最佳的总压比.  相似文献   

9.
本文研究恒温和变温热源条件下具有等熵压缩、膨胀过程的闭式燃气轮机回热循环有限时间热力学性能,导出两种情况下的功率输出和热效率与循环压比间的关系,由此可得最佳功率、效率特性.对于给定的热源条件,回热对循环功率有很大影响,这一结论与经典的分析明显不同.分析中计入了工质与高、低温热源间换热器和回热器的热阻损失.当不计高、低温侧换热器的热阻损失时,本文结果与经典结论一致.  相似文献   

10.
本文研究恒温和变温热源条件下具有等熵压缩、膨胀过程的闭式燃气轮机回热循环有限时间热力 学性能,导出两种情况下的功率输出和热效率与循环压比间的关系,由此可得最佳功率、效率特性。对于给定的热源条件,回热对循环功率有很大影响,这一结论与经典的分析明显不同。分析中计入了工质与高,低温热源间换热器和回热器的热阻损失,当不计高、低温侧换热器的热阻损失时,本文结果与经典结论一致。  相似文献   

11.
In this paper, power is optimized for an endoreversible closed intercooled regenerated Brayton cycle coupled to constant-temperature heat reservoirs in the viewpoint of finite-time thermodynamics (FTT) or entropy generation minimization (EGM). The effects of some design parameters, including the cycle heat reservoir temperature ratio and total heat exchanger inventory, on the maximum power and the corresponding efficiency are analyzed by numerical examples. The analysis shows that the cycle dimensionless power can be optimized by searching the optimum heat conductance distributions among the hot- and cold-side heat exchangers, the regenerator and the intercooler for fixed total heat exchanger inventory, and by searching the optimum intercooling pressure ratio. When the optimization is performed with respect to the total pressure ratio of the cycle, the maximum dimensionless power can be maximized again.  相似文献   

12.
《Applied Energy》2005,82(2):181-195
In this paper, in the viewpoint of finite-time thermodynamics and entropy-generation minimization are employed. The analytical formulae relating the power and pressure-ratio are derived assuming heat-resistance losses in the four heat-exchangers (hot- and cold-side heat exchangers, the intercooler and the regenerator), and the effect of the finite thermal-capacity rate of the heat reservoirs. The power optimization is performed by searching the optimum heat-conductance distributions among the four heat-exchangers for a fixed total heat-exchanger inventory, and by searching for the optimum intercooling pressure-ratio. When the optimization is performed with respect to the total pressure-ratio of the cycle, the maximum power is maximized twice and a ‘double-maximum’ power is obtained. When the optimization is performed with respect to the thermal capacitance rate ratio between the working fluid and the heat reservoir, the double-maximum power is maximized again and a thrice-maximum power is obtained. The effects of the heat reservoir’s inlet-temperature ratio and the total heat-exchanger inventory on the optimal performance of the cycle are analyzed by numerical examples.  相似文献   

13.
考虑热阻损失、压缩机与膨胀机的内损失及管路系统的压力损失,研究一个比较接近实际装置的回热式交温热源空气制冷循环,得出了循环容积制冷率制冷系数的解析关系式。由数值计算分析了压比、热导率分配以及工质与热源间的热容率匹配等参数对容积制冷率的影响。  相似文献   

14.
The performance of an irreversible closed intercooled regenerator Brayton-cycle coupled to constant-temperature heat reservoirs is analyzed by using the theory of finite-time thermodynamics (FTT). Analytical formulae for dimensionless power and efficiency are derived. Especially, the intercooling pressure-ratio is optimized for the optimal power and the optimal efficiency, respectively. The effects of component (the intercooler, the regenerator, and the hot- and cold-side heat-exchangers) effectivenesses, the compressor and turbine efficiencies, the heat-reservoir temperature-ratio, and the temperature ratio of the cooling fluid in the intercooler and the cold-side heat reservoir on the optimal power and the corresponding efficiency and corresponding intercooling pressure ratio, as well as the optimal efficiency and the corresponding power and corresponding intercooling pressure-ratio are analyzed by detailed numerical examples.  相似文献   

15.
Entropy generation minimization technique is used in the analysis of an irreversible closed intercooled regenerative Brayton cycle coupled to variable-temperature heat reservoirs. Mathematical models are developed for dimensionless power and efficiency for a multi-stage Brayton cycle. The dimensionless power and efficiency equations are used to analyze the effects of total pressure ratio, intercooling pressure ratio, thermal capacity rates of the working fluid and heat reservoirs, and the component (regenerator, intercooler, hot- and cold-side heat exchangers) effectiveness. Using detailed numerical examples, the optimal power and efficiency corresponding to variable component effectiveness, compressor and turbine efficiencies, intercooling pressure ratio, total pressure ratio, pressure recovery coefficients, heat reservoir inlet temperature ratio, and the cooling fluid in the intercooler and the cold-side heat reservoir inlet temperature ratio are analyzed.  相似文献   

16.
《Exergy》2002,2(4):380-386
The performance optimization of an endoreversible Braysson cycle with heat resistance losses in the hot- and cold-side heat exchangers is performed by using finite-time thermodynamics. The relations between the power output and the working fluid temperature ratio, between the power density and the working fluid temperature ratio, as well as between the efficiency and the working fluid temperature ratio of the cycle coupled to constant-temperature heat reservoirs are derived. Moreover, the optimum heat conductance distributions corresponding to the optimum dimensionless power output, the optimum dimensionless power density and the optimum thermal efficiency of the cycle, and the optimum working fluid temperature ratios corresponding to the optimum dimensionless power output and the optimum dimensionless power density are provided. The effects of various design parameters on those optimum values are studied by detailed numerical examples.  相似文献   

17.
This paper analyses the performance of a real heat pump plant via methods of entropy generation minimization or finite‐time thermodynamics. The analytical relations between heating load and pressure ratio, and between coefficient of performance (COP) and pressure ratio of real closed regenerated Brayton heat pump cycles coupled to constant‐ and variable‐temperature heat reservoirs are derived. In the analysis, the irreversibilities include heat transfer‐irreversible losses in the hot‐ and cold‐side heat exchangers and the regenerator, the non‐isentropic expansion and compression losses in the compressor and expander, and the pressure drop loss in the pipe and system. The optimal performance characteristics of the cycle may be obtained by optimizing the distribution of heat conductances or heat transfer surface areas among the two heat exchangers and the regenerator, and the matching between working fluid and the heat reservoirs. The influence of the effectiveness of regenerator, the effectiveness of hot‐ and cold‐side heat exchangers, the efficiencies of the expander and compressor, the pressure recovery coefficient and the temperature of the heat reservoirs on the heating load and COP of the cycle are illustrated by numerical examples. Published in 1999 by John Wiley & Sons, Ltd.  相似文献   

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