A Supercritical Reactive Separation Process to Obtain Biopesticides (phorbol-esters) in the Biodiesel Production from Jatropha curcas Oil

被引:0
作者
Perez-Cisneros, Eduardo S. [1 ,2 ]
Sales-Cruz, Mauricio [3 ]
Rodriguez-Lopez, Veronica [4 ]
Mena-Espino, Xenia [1 ]
Viveros-Garcia, Tomas [1 ]
机构
[1] Univ Autonoma Metropolitana Iztapalapa, Dept Ingn Proc & Hidraul, Av San Rafael Atlixco 186, Mexico City 09340, DF, Mexico
[2] Univ Autonoma Metropolitana Iztapalapa, Energia & Medio Ambiente, Av San Rafael Atlixco 186, Mexico City 09340, DF, Mexico
[3] Univ Autonoma Metropolitana Cuajimalpa, Dept Proc & Tecnol, Artificios 40, Mexico City 01120, DF, Mexico
[4] Univ Autonoma Estado Morelos, Fac Farm, Cuernavaca, Morelos, Mexico
来源
26TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING (ESCAPE), PT B | 2016年 / 38B卷
关键词
Biodiesel; biopesticide; Jatropha Curcas; supercritical reactive-separation process;
D O I
10.1016/B978-0-444-63428-3.50308-8
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A coupled supercritical extraction and reactive distillation processes for the extraction of the phorbol ester (biopesticide) and to produce biodiesel from Jatropha Curcas oil has been developed. Simulations of the extractive-reactive processes in Aspen-Plus environment were performed using the PC-SAFT equation of state. The pure component properties of the phorbol-ester are determined using the group contribution method of Marrero and Gani (2001). Simulation results show that a supercritical solvent mixture of CO2 and methanol is the appropriate solvent for enhanced phorbol ester extraction. A 20 equilibrium stages supercritical extractive column (SEC) under a total pressure of 5 bars and a solvent mixture of CO2/methanol was designed to separate the phorbol ester. The SEC is further coupled to the integrated reactive-distillation process for production of biodiesel.
引用
收藏
页码:1821 / 1826
页数:6
相关论文
共 6 条
[1]  
Annesini Maria C., 2014, CHEM ENG T, V38, P67
[2]  
Becker K, 1998, VET HUM TOXICOL, V40, P82
[3]   Perturbed-chain SAFT: An equation of state based on a perturbation theory for chain molecules [J].
Gross, J ;
Sadowski, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (04) :1244-1260
[4]   Group-contribution based estimation of pure component properties [J].
Marrero, J ;
Gani, R .
FLUID PHASE EQUILIBRIA, 2001, 183 :183-208
[5]  
Perez-Cisneros Eduardo S., 2015, 12 INT S PROC SYST E, P1013
[6]  
Rao D. M., 2012, JATROPHA CHALLENGES, P369