A generalized neural network model for the VLE of supercritical carbon dioxide fluid extraction of fatty oils

被引:10
作者
Aminian, Ali [1 ]
ZareNezhad, Bahman [1 ]
机构
[1] Semnan Univ, Fac Chem Petr & Gas Engn, POB 35195-63, Semnan, Iran
关键词
Neural network; SC-CO2 fluid extraction; Purification; Fatty oils; VAPOR-LIQUID-EQUILIBRIA; PRESSURE PHASE-EQUILIBRIA; BINARY-MIXTURES; OLEIC-ACID; SYSTEMS; CO2; DENSITIES; BEHAVIOR; WATER; ESTERS;
D O I
10.1016/j.fuel.2020.118823
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In the present work, a neural network (NN) model was developed for the precise prediction of the phase behavior of supercritical carbon dioxide (SC-CO2) and fatty oils. A total of 678 SC-CO2 + fatty oils vapor-liquid equilibrium datasets for fatty acids, methyl and ethyl esters plus 120 data points for further accuracy examinations were used. The Cascade-Forward scheme was used as the basic architecture for the NN model calculations and predictions. Comparison between the values of the average absolute deviation of the NN model and the most important existing models showed that the NN model outperforms the other alternatives. The overall AAD for CO2 mole fractions in liquid and vapor phases were obtained to be 1.516 and 0.312%, respectively.
引用
收藏
页数:9
相关论文
共 34 条
[1]   Accurate predicting the viscosity of biodiesels and blends using soft computing models [J].
Aminian, Ali ;
ZareNezhad, Bahman .
RENEWABLE ENERGY, 2018, 120 :488-500
[2]  
[Anonymous], 2005, Biomimicry for optimization, control, and automation
[3]   Phase behavior measurement for the system CO2 + glycerol plus ethanol at high pressures [J].
Araujo, Odilon A. S. ;
Ndiaye, Papa M. ;
Ramos, Luiz P. ;
Corazza, Marcos L. .
JOURNAL OF SUPERCRITICAL FLUIDS, 2012, 62 :41-46
[4]   High-pressure (vapor plus liquid) equilibrium in binary mixtures of (carbon dioxide plus water or acetic acid) at temperatures from 313 to 353 K [J].
Bamberger, A ;
Sieder, G ;
Maurer, G .
JOURNAL OF SUPERCRITICAL FLUIDS, 2000, 17 (02) :97-110
[5]   VAPOR LIQUID EQUILIBRIA FOR BINARY-MIXTURES OF CARBON-DIOXIDE AND FATTY-ACID ETHYL-ESTERS [J].
BHARATH, R ;
INOMATA, H ;
ARAI, K ;
SHOJI, K ;
NOGUCHI, Y .
FLUID PHASE EQUILIBRIA, 1989, 50 (03) :315-327
[6]   PHASE-EQUILIBRIA OF SUPERCRITICAL CO2 - FATTY OIL COMPONENT BINARY-SYSTEMS [J].
BHARATH, R ;
YAMANE, S ;
INOMATA, H ;
ADSCHIRI, T ;
ARAI, K .
FLUID PHASE EQUILIBRIA, 1993, 83 :183-192
[7]   Phase behavior and modeling of supercritical carbon dioxide-organic acid mixtures [J].
Byun, HS ;
Kim, K ;
McHugh, MA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (12) :4580-4587
[8]   Vapor-liquid equilibria and densities of CO2 with four unsaturated fatty acid esters at elevated pressures [J].
Chang, CMJ ;
Lee, MS ;
Li, BC ;
Chen, PY .
FLUID PHASE EQUILIBRIA, 2005, 233 (01) :56-65
[9]   Vapor-liquid equilibria of carbon dioxide with linoleic acid, α-tocopherol and triolein at elevated pressures [J].
Chen, CC ;
Chang, CMJ ;
Yang, PW .
FLUID PHASE EQUILIBRIA, 2000, 175 (1-2) :107-115
[10]   Vapor-liquid equilibria of carbon dioxide with diethyl oxalate, ethyl laurate, and dibutyl phthalate binary mixtures at elevated pressures [J].
Cheng, KW ;
Tang, MI ;
Chen, YP .
FLUID PHASE EQUILIBRIA, 2001, 181 (1-2) :1-16