为了适应节能与环境保护的需求,研究了一种适用于自复叠制冷系统的新型绿色混合制冷工质(R290/R744)的汽液相平衡特性。根据相平衡条件采用PT状态方程结合Van der Waals混合规则推导出该混合制冷工质的相平衡计算式,通过软件编程计算了...为了适应节能与环境保护的需求,研究了一种适用于自复叠制冷系统的新型绿色混合制冷工质(R290/R744)的汽液相平衡特性。根据相平衡条件采用PT状态方程结合Van der Waals混合规则推导出该混合制冷工质的相平衡计算式,通过软件编程计算了两种有工程实用意义的相平衡问题,一种是已知混合物压力和液相摩尔分数,计算泡点温度和气相摩尔分数;另一种是已知混合物压力和气相摩尔分数,计算露点温度和液相摩尔分数,并根据计算数据绘制了汽液平衡曲线。数据显示最大相对误差为4.840%,最小相对误差为0.005%。计算结果表明,采用给出的R290/R744混合制冷剂相平衡计算式具有较高的计算精度,从而为采用该混合制冷剂的自复叠制冷循环研究奠定基础。展开更多
采用pT状态方程并结合van der Waals混合规则,对R290/R744混合物的热物性参数进行了理论研究,计算中采用了Kay规则计算的虚拟临界参数来代替混合物的真实临界参数,计算得到了R290/R744混合物饱和气体比容、饱和液体密度、比焓和比熵等...采用pT状态方程并结合van der Waals混合规则,对R290/R744混合物的热物性参数进行了理论研究,计算中采用了Kay规则计算的虚拟临界参数来代替混合物的真实临界参数,计算得到了R290/R744混合物饱和气体比容、饱和液体密度、比焓和比熵等物性参数,并对计算数据进行了精度分析.计算结果为R290/R744混合物的应用打下了基础.展开更多
Low critical temperature limits the application of CO_2 trans-critical power cycle.The binary mixture of R290/CO_2has higher critical temperature.Using mixture fluid may solve the problem that subcritical CO_2 is hard...Low critical temperature limits the application of CO_2 trans-critical power cycle.The binary mixture of R290/CO_2has higher critical temperature.Using mixture fluid may solve the problem that subcritical CO_2 is hardly condensed by conventional cooling water.In this article,theoretical analysis is executed to study the performance of the zeotropic mixture for trans-critical power cycle using low-grade liquid heat source with temperature of200℃.The results indicated that the problem that CO_2 can't be condensed in power cycle by conventional cooling water can be solved by mixing R290 to CO_2.Variation trend of outlet temperature of thermal oil in supercritical heater with heating pressure is determined by the composition of the mixture fluid.Gliding temperature causes the maximum outlet temperature of cooling water with the increase of mass fraction of R290.There are the maximum values for cycle thermal efficiency and net power output with the increase of supercritical heating pressure.展开更多
文摘为了适应节能与环境保护的需求,研究了一种适用于自复叠制冷系统的新型绿色混合制冷工质(R290/R744)的汽液相平衡特性。根据相平衡条件采用PT状态方程结合Van der Waals混合规则推导出该混合制冷工质的相平衡计算式,通过软件编程计算了两种有工程实用意义的相平衡问题,一种是已知混合物压力和液相摩尔分数,计算泡点温度和气相摩尔分数;另一种是已知混合物压力和气相摩尔分数,计算露点温度和液相摩尔分数,并根据计算数据绘制了汽液平衡曲线。数据显示最大相对误差为4.840%,最小相对误差为0.005%。计算结果表明,采用给出的R290/R744混合制冷剂相平衡计算式具有较高的计算精度,从而为采用该混合制冷剂的自复叠制冷循环研究奠定基础。
文摘采用pT状态方程并结合van der Waals混合规则,对R290/R744混合物的热物性参数进行了理论研究,计算中采用了Kay规则计算的虚拟临界参数来代替混合物的真实临界参数,计算得到了R290/R744混合物饱和气体比容、饱和液体密度、比焓和比熵等物性参数,并对计算数据进行了精度分析.计算结果为R290/R744混合物的应用打下了基础.
基金Project 51306198 supported by the National Natural Science Foundation of China
文摘Low critical temperature limits the application of CO_2 trans-critical power cycle.The binary mixture of R290/CO_2has higher critical temperature.Using mixture fluid may solve the problem that subcritical CO_2 is hardly condensed by conventional cooling water.In this article,theoretical analysis is executed to study the performance of the zeotropic mixture for trans-critical power cycle using low-grade liquid heat source with temperature of200℃.The results indicated that the problem that CO_2 can't be condensed in power cycle by conventional cooling water can be solved by mixing R290 to CO_2.Variation trend of outlet temperature of thermal oil in supercritical heater with heating pressure is determined by the composition of the mixture fluid.Gliding temperature causes the maximum outlet temperature of cooling water with the increase of mass fraction of R290.There are the maximum values for cycle thermal efficiency and net power output with the increase of supercritical heating pressure.
文摘基于传热和压降的耦合作用,针对R744/R290(20/80)和R125/R290(25/75)混合工质逆流换热冷凝器建立基于熵产最小化的管长优化数学模型,并结合Cavallini凝换热性能评价指标PEI(performance evaluation index)和温度惩罚因子TTP(total temperature penalization),得到了混合工质PEI与传热系数α之间的函数关系,具体分析了管径、冷凝温度和被动压降对管长优化结果的影响。研究表明,制冷剂饱和温度降为制冷剂与壁面之间传热驱动温差的0.6倍,高压工质R744/R290(20/80)(临界温度低的工质)的PEI值更小,冷凝换热性能更优,同时小管径的冷凝器最优管长更小,且最优管长随随着冷凝温度的增大而增大,随着被动压降的增加而减小。