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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2024, Vol. 18 Issue (11): 130   https://doi.org/10.1007/s11705-024-2482-5
  本期目录
Extractive distillation of cycloalkane monomers from the direct coal liquefaction fraction
Shuo-Shuo Zhang1,2, Xing-Bao Wang1,2(), Wen-Ying Li1()
1. State Key Laboratory of Clean and Efficient Coal Utilization, Taiyuan University of Technology, Taiyuan 030024, China
2. College of Chemical Engineering and Technology, Taiyuan University of Technology, Taiyuan 030024, China
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Abstract

Separating monomeric cycloalkanes from naphtha obtained from direct coal liquefaction not only facilitates the valuable utilization of naphtha but also holds potential for addressing China’s domestic chemical feedstock market demand for these compounds. In extractive distillation processes of naphtha, relative volatility serves as a crucial parameter for extractant selection. However, determining relative volatility through conventional vapor-liquid equilibrium experiments for extractant selection proves challenging due to the complexity of naphtha’s compound composition. To address this challenge, a prediction model for the relative volatility of n-heptane/methylcyclohexane in various extractants has been developed using machine-learning quantitative structure-property relationship methods. The model enables rapid and cost-effective extractant selection. The statistical analysis of the model revealed favorable performance indicators, including a coefficient of determination of 0.88, cross-validation coefficient of 0.94, and root mean square error of 0.02. Factors such as α, EHOMO, ρ, and logPoct/water collectively influence relative volatility. Analysis of standardized coefficients in the multivariate linear regression equation identified density as the primary factor affecting the relative volatility of n-heptane/methylcyclohexane in the different extractants. Extractants with higher densities, devoid of branched chains, exhibited increased relative volatility compared to their counterparts with branched chains. Subsequently, the process of separating cycloalkane monomers from direct coal liquefaction products via extractive distillation was optimized using Aspen Plus software, achieving purities exceeding 0.99 and yields exceeding 0.90 for cyclohexane and methylcyclohexane monomers. Economic, energy consumption, and environmental assessments were conducted. Salicylic acid emerged as the most suitable extractant for purifying cycloalkanes in direct coal liquefaction naphtha due to its superior separation effectiveness, cost efficiency, and environmental benefits. The tower parameters of the simulated separation unit provide valuable insights for the design of actual industrial equipment.

Key wordsnaphtha    relative volatility    molecular descriptor    quantitative structure-property relationship model
收稿日期: 2024-03-30      出版日期: 2024-07-19
Corresponding Author(s): Xing-Bao Wang,Wen-Ying Li   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2024, 18(11): 130.
Shuo-Shuo Zhang, Xing-Bao Wang, Wen-Ying Li. Extractive distillation of cycloalkane monomers from the direct coal liquefaction fraction. Front. Chem. Sci. Eng., 2024, 18(11): 130.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-024-2482-5
https://academic.hep.com.cn/fcse/CN/Y2024/V18/I11/130
Fig.1  
Fig.2  
Fig.3  
Fig.4  
Variable R2traina) RMSEtrainb) R2valc) RMSEvald)
α 0.31 0.04 0.16 0.11
α, logPoct/water 0.32 0.04 0.24 0.11
α, logPoct/water, ρ 0.48 0.04 0.29 0.08
α, logPoct/water, ρ, EHOMO 0.88 0.02 0.74 0.05
α, logPoct/water, ρ, EHOMO, ELUMO 0.88 0.02 0.60 0.06
Tab.1  
Independent variable Unstandardized coefficient Standardized coefficient ta) pb) VIF
Constant 1.389 24.204 0.000
α/a.u. ?0.001 ?0.449 ?5.665 0.000 1.212
EHOMO/eV 0.041 0.554 7.203 0.000 1.141
ρ/(g·cm?3) 0.211 0.614 7.924 0.000 1.160
logPoct/water/(kg·mol?1) ?0.007 ?0.232 ?2.986 0.006 1.167
Tab.2  
Fig.5  
Number R2 RMSE D-W Q2
Fitting model 32 0.88 0.02 2.20 0.94
Training set 24 0.74 0.05 2.31 0.92
Validation set 8 0.85 0.02 2.18 0.89
Tab.3  
Fig.6  
Fig.7  
AF The surface area corresponding to an equivalent surface with an electron density of 0.001 a.u. when the molecule is in the gas phase, ?2
EHOMO Energy of the highest occupied molecular orbital, eV
ELUMO Energy of the lowest unoccupied molecular orbital, eV
logPoct/water Partition coefficient of molecules in n-octanol-water, kg·mol?1
SASA Solvent accessible biomolecular surface area, ?2
V The volume corresponding to an equivalent surface with an electron density of 0.001 a.u. when the molecule is in the gas phase, ?3
α Molecular polarizability, a.u.
ρ The density corresponding to an equivalent surface with an electron density of 0.001 a.u. when the molecule is in the gas phase, g·cm?3
  
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