共查询到18条相似文献,搜索用时 187 毫秒
1.
2.
基于基团贡献法的思想,本文采用改进的SRK状态方程和修正的MHV1混合规则,将UNIFAC基团贡献法扩展用于HFC HC二元混合物气液相平衡性质的描述,给出了基团划分表和基团间的相互作用参数,使用该方法可以较好地再现HFC HC二元混合物的气液相平衡性质,并且具有良好的预测效果. 相似文献
3.
HFC/HC混合工质的气液性平衡实验研究结果表明,该类型混合工质大多存在共沸现象。根据形成共沸点的热力学条件,以PR状态方程结合vdW混合法则,利用建立的二元相互作用系数kij差值关联模型,对10种HFCs工质(HFC23、HFC32、HFC125、HFC143a、HFC134a、HFC152a、HFC227ea、HFC236fa、HFC236ea、HFC245fa)与3种HCs工质(HC290、HC600a、HC600)相互组合而成的30种HFC/HC混合工质进行了共沸点判断和共沸点性质推算,并与已有气液相平衡实验数据的体系进行对比。结果表明该方法可用于推算HFC/HC混合工质共沸点性质。 相似文献
4.
1引言在混合替代工质的研究中,要分析其热力学性质和循环性能,必须有能够准确描述混合制冷剂性质的状态方程。目前计算采用的各种混合状态方程都必需有混合物各组分间的二元交互作用系数Kij。Kij的值一般需要由回归二元混合工质的PVTx实验数据或相平衡数据而得到。实际的混合工质替代研究中,常常没有或缺少混合物的实验数据。对于二元混合物而言,其热力性质应与组成这种混合物的两种纯质的性质密切相关,有可能以纯质的物性来表达混合物的性能,而大多数纯质制冷剂都有用实验数据回归的精度很高的专用状态方程和蒸气压方程。所以,如… 相似文献
5.
醇+卤代烃混合体系,尤其是乙醇、三氟乙醇(TFE)等与卤代烃的混合工质在吸收式制冷、热泵、蒸气动力循环等领域中有着重要的应用.CPA方程可以描述缔合流体的性质,用于含醇类组元的混合体系气液相平衡性质描述.本文首先从纯物质饱和性质实验数据回归得到了CPA方程参数;将CPA方程应用于醇+卤代烃混合体系的气液相平衡计算,采用并比较了2种缔合方案;比较了CPA方程与G~E-EoS模型的相平衡计算效果.CPA状态方程在揭示分子间相互作用的基础上可准确描述醇+卤代烃混合体系的气液相平衡性质. 相似文献
6.
本文引入一种基于基团贡献的逸度系数模型来解决常规模型对非共沸混合制冷剂气液相平衡预测精度不足的问题,该模型只使用较少的共性基团参数就能推算大量多元混合物的物性.使用PR状态方程结合vdW混合规则来描述气相逸度、UNI-FAC模型来描述液相逸度.通过对R32+R236fa非共沸混合工质对的气液相平衡饱和蒸汽压力进行计算,并将结果与实验数据、REFPROP 8.0商业软件计算值对比分析.结果 表明:本文模型比REFPROPS.0软件更适应于混合工质;此外,该模型只考虑基团间相互作用,简化了热物性计算.基于提出的模型,绘制了R32+R236fa非共沸混合工质在278.15~363.15 K的相图. 相似文献
7.
基于制冷剂物性计算软件NIST REFPROP 7.0及R125/R600a气液相平衡实验数据,使用MBWR状态方程结合Lemmon-Jacobsen混合物模型,对R125/R600a(50/50 mass%)混合替代工质的热力学性质进行了计算,并制作给出了其压焓图(p-h)、温熵图(T-s)和比定压热容图(c<,p>-T)及饱和性质表.最后理论计算分析了其空调制冷工况的性能,结果表明该混合工质具有与R22相当的压缩比和COP值,比R22较低的排气温度和较高的单位质量制冷量. 相似文献
8.
9.
10.
11.
12.
利用密度平移的方法对Peng-Robinson状态方程计算的液相密度进行了修正,给出了其描述平移量的关联式。对22种卤代烃纯物质的计算结果表明,修正后的PR方程能够很好地计算液相密度,并且能很好地再现纯物质的临界压缩因子,计算精度可以满足工程应用的需要。 相似文献
13.
HFC混合物表面张力的预估方程 总被引:1,自引:1,他引:0
表面张力是有沸腾和凝结换热计算必不可少的物性参数,目前国际上已商业化使用或提出的潜在的环保工质,大多数为氢氟烃(HFC)混合物,尤其是R22和R502的替代物、本文应用对比态原理和重正化群理论,提出了一种新的HFC类物质混合物表面张力的预估方程,并与国际上现有的预估式进行了比较分析。新预估式可以在广阔的温度范围内较高精度地再现实验数据,计算精度可以满足工程应用的需要. 相似文献
14.
The equation of state (EOS) for hard-sphere fluid derived from compressibility routes of Percus-Yevick theory (PYC) is extended. The two parameters are determined by fitting well-known virial coefficients of pure fluid. The extended cubic EOS can be directly extended to multi-component mixtures, merely demanding the EOS of mixtures also is cubic and combining two physical conditions for the radial distribution functions at contact (RDFC) of mixtures. The calculated virial coefficients of pure fluid and predicted compressibility factors and RDFC for both pure fluid and mixtures are excellent as compared with the simulation data. The values of RDFC for mixtures with extremely large size ratio 10 are far better than the BGHLL expressions in literature. 相似文献
15.
The equation of state(EOS) for hard-sphere fluid derived from compressibility routes of Percus-Yevick theory(PYC) is extended. The two parameters are determined by fitting well-known virial coefficients of pure fluid.The extended cubic EOS can be directly extended to multi-component mixtures, merely demanding the EOS of mixtures also is cubic and combining two physical conditions for the radial distribution functions at contact(RDFC) of mixtures.The calculated virial coefficients of pure fluid and predicted compressibility factors and RDFC for both pure fluid and mixtures are excellent as compared with the simulation data. The values of RDFC for mixtures with extremely large size ratio 10 are far better than the BGHLL expressions in literature. 相似文献
16.
The nucleate pool boiling heat transfer data on a smooth flat surface were measured for three binary mixtures of HC600a/HFC134a, HC600a/HC290, and HC600a/HFC23. Much effort was made to investigate the influence of the boiling range on the pool-boiling heat transfer performance. From the experimental results, the HC600a/HFC23 mixture with a wide boiling range showed lower heat transfer coefficients (HTCs) than the mixture with a narrow boiling range such as HC600a/HFC134a and HC600a/HC290 systems. The measured data were also compared with the results predicted by five well-known correlations. It can be found that the average deviation is less than 25% for mixtures with narrow boiling ranges, but a larger deviation for mixtures with wide boiling ranges. 相似文献
17.
《Journal of Molecular Liquids》2006,123(2-3):134-138
In this paper, an analytical equation of state (EoS) proposed by Ihm–Song–Mason (ISM) was employed to calculate the molar volume of mixtures of methane with krypton, argon, ethane and carbon monoxide. The best available pair interaction potential energy has been used to evaluate the second virial coefficients required by the ISM EoS. The calculated values of second virial coefficients were applied to the ISM EOS to predict the molar volumes for the above mentioned mixtures. Agreement with the experiment is excellent for all systems. 相似文献