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首页> 外文期刊>Chemical Engineering & Technology: Industrial Chemistry -Plant Equipment -Process Engineering -Biotechnology >Croup Contribution Method Based on UNIFAC Croups for the Estimation of Vapor Pressures of Pure Hydrocarbon Compounds
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Croup Contribution Method Based on UNIFAC Croups for the Estimation of Vapor Pressures of Pure Hydrocarbon Compounds

机译:基于UNIFAC溃疡估计纯烃类化合物蒸汽压力的CROUP贡献方法

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A group contribution method based on UNIFAC groups was developed to estimate the vapor pressures of pure hydrocarbons at reduced temperatures (0.45-0.95). The maximum pressure for the correlation is 35atm. Experimental vapor pressures for 456 hydrocarbons were collected and used to calculate model parameters. The developed model utilizes the combinatorial and the residual UNIFAC terms and the fugacity of pure hydrocarbons. The model parameters were fitted in two modes, using contributions from first-order groups. In the first case, the Gibbs free energy was considered only as an explicit function of temperature, and in the second one, in addition to the temperature effect, the effect of the molecular structure was also considered. Taking the molecular structure into account significantly decreases the prediction error. Hence, a uniform linear relationship to structure is considered. In the modified models, the error in prediction of the vapor pressure in the temperature range discussed is less than 15%.
机译:开发了一种基于UNIFAC组的组贡献方法,以估计在降低温度下纯烃的蒸汽压力(0.45-0.95)。相关性的最大压力为35ATM。收集456个烃的实验蒸汽压力并用于计算模型参数。开发的模型利用组合和残留的Unifac术语和纯烃的不足。模型参数以两种模式配备,使用一阶组的贡献。在第一种情况下,Gibbs自由能仅被认为是温度的明确功能,并且在第二个中,除了温度效应之外,还考虑了分子结构的效果。考虑分子结构显着降低预测误差。因此,考虑与结构的均匀线性关系。在修改模型中,讨论的温度范围内的蒸气压的预测误差小于15%。

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