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1.
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   

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.
计入工质与高低浊侧换热器、回热器和中冷器的热阻损失以功率为优化目标,借助数值计算,研究了变温热源条件下内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比与总压比的关系;分析了工质与热源间的热容率匹配对双重最大功率的影响。  相似文献   

4.
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   

5.
以功率密度——循环输出功率与最大比容之比——作为优化目标。用有限时间热力学方法 ,对恒温热源条件下内可逆闭式燃气轮机循环的高、低温侧换热器的热导率分配进行了优化。由数值算例给出了循环的一些主要特征参数对热导率最优分配和最大功率密度的影响 ,以及功率密度最大时的最佳热导率分配与最佳压比之间的对应关系。  相似文献   

6.
恒温热源不可逆闭式中冷回热燃气轮机循环的功率和效率   总被引:4,自引:0,他引:4  
用有限时间热力学方法首次研究了恒温热源条件下不可逆闭式中冷回热燃气轮机循环的功率、效率以及中间压比特性,导出了无因次功率及效率的解析式。通过数值计算方法,分析了中冷度、回热度对循环最优功率、最优效率及其对应的中间压比分配的影响。  相似文献   

7.
恒温热源条件下内不可逆布雷顿循环的功率密度特性   总被引:1,自引:0,他引:1  
用有限时间热力学方法分析恒温热源条件下不可逆布雷顿循环的功率密度特性,计入工质与高、低温侧换热器的热阻损失及压气机、透平的不可逆压缩和膨胀损失,导出了功率密度与压比间的解析式,并通过数值计算将对应于最大功率密度时的一些参数与对应于最大功率时的同样参数进行了比较,说明了功率密度设计的优点与不足.  相似文献   

8.
提出了回热式布雷顿-两平行逆布雷顿联合循环模型。对该模型进行了第一定律性能分析与优化,得出了该循环最优效率和最优比功的表达式,分析了回热度及其他参数对联合循环最优热效率和最优比功的影响。分析表明,增加回热器后能提高联合循环的热效率,但此时联合循环的输出比功较小。  相似文献   

9.
10.
相对于已有的高温工质进入回热器回热后再进入底循环做功的回热式布雷顿-逆布雷顿联合循环模型,本文提出了一种新型的高温工质在底循环做功后再进入回热器回热的回热式布雷顿-逆布雷顿联合循环模型。对两种回热式布雷顿-逆布雷顿联合循环进行了第一定律性能分析与优化,得出了两种联合循环的最优热效率和最优比功的表达式,比较了两种联合循环的热效率及比功特性,并分析了回热器有效度对两种联合循环最优热效率和最优比功的影响。分析表明,增加回热器后能提高两种联合循环的热效率,与已有的联合循环相比,新型联合循环能在其顶循环压气机压比较小的情况下获得较大的热效率和比功。  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.
This paper describes an application of finite‐time thermodynamics to optimize the power output of endoreversible intercooled Brayton cycles coupled to two heat reservoirs with infinite thermal capacitance rates. The effects of intercooling on the maximum power and maximum‐power efficiency of an endoreversible Brayton cycle are examined. With appropriate temperature ratios of turbines and compressors being used, the maximum power output of an endoreversible intercooled Brayton cycle can be higher than that of an endoreversible simple Brayton cycle without lowering the thermal efficiency. New diagrams for maximum power, maximum‐power thermal efficiency, and optimum temperature ratios of turbines and compressors are reported. Copyright © 2000 John Wiley & Sons, Ltd.  相似文献   

13.
《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   

14.
An endoreversible closed modified simple Brayton cycle model with isothermal heat addition coupled to variable-temperature heat reservoirs is established using finite-time thermodynamics. Analytical expressions of dimensionless power output, thermal efficiency, dimensionless entropy generation rate and dimensionless ecological function are derived. Influences of cycle thermodynamic parameters on ecological performance and optimal compressor pressure ratio, optimal power output, optimal cycle thermal efficiency and optimal entropy generation rate corresponding to maximum ecological function are obtained and compared with those corresponding to maximum power output. The results show that cycle thermal efficiency improvement and entropy generation rate reduction are obtained at the expense of higher compressor pressure ratio and a little sacrifice of power output at maximum ecological function. The compromises between power output and entropy generation rate and between power output and cycle thermal efficiency, respectively, are achieved.  相似文献   

15.
用有限时间热力学方法建立了一个工作在恒温热源TH、TL之间,存在热阻、热漏和再热的定常流空气标准闭式布雷顿循环模型。导出了其功率、效率的一般关系并对其进行优化,得到循环的基本优化关系;分析了在傅立叶导热定律下再热对循环最优性能的影响。  相似文献   

16.
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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