Exergy Load Distribution Analysis Applied to the Dehydration of Ethanol by Extractive Distillation

被引:7
|
作者
Guerrero-Martin, Camilo Andres [1 ,2 ,3 ]
Fernandez-Ramirez, Juan Sebastian [4 ]
Arturo-Calvache, Jaime Eduardo [5 ]
Milquez-Sanabria, Harvey Andres [5 ]
Fernandes, Fernando Antonio da Silva [2 ]
Gomes, Vando Jose Costa [1 ,2 ,3 ]
Lima e Silva, Wanessa [1 ,2 ,3 ]
Duarte, Emanuele Dutra Valente [1 ,2 ,3 ]
Guerrero-Martin, Laura Estefania [1 ]
Lucas, Elizabete Fernandes [6 ,7 ]
机构
[1] Fed Univ Para, Fac Petr Engn, LOTEP Lab Operacoes & Tecnol Energet Aplicadas Ind, BR-66075110 Salinopolis, Brazil
[2] Fed Univ Para, Dept Engn, Campus Salinopolis,Rua Raimundo Santana Cruz 9 S-N, BR-68721000 Salinopolis, Brazil
[3] Fed Univ Para, Fac Petr Engn, LEEPER Lab Ensino Engn Poco & Reservatorio, BR-68721000 Salinopolis, Brazil
[4] Univ Nacl Colombia, Dept Ingn Quim & Ambiental, Bogota 111321, Colombia
[5] Fdn Univ Amer, Dept Ingn Quim & Ambiental, Bogota 111221, Colombia
[6] Univ Fed Rio de Janeiro, Met & Mat Engn Program, COPPE, LADPOL, Av Horacio Macedo 2030,Bloco F, BR-21941598 Rio De Janeiro, Brazil
[7] Univ Fed Rio de Janeiro, Inst Macromol, LMCP, Rua Moniz Aragao 360,Bloco 8G-CT2, BR-21941594 Rio De Janeiro, Brazil
关键词
exergy load distribution; exergy efficiency; dehydration of ethanol; extractive distillation; BIOMASS GASIFICATION; ENERGY; OPTIMIZATION; PYROLYSIS; SIMULATION; CONVERSION; PLANT; WATER;
D O I
10.3390/en16083502
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
This study presents the analysis of the exergy load distribution in a separation process by extractive distillation for ethanol dehydration. The methodology carried out is divided into three parts: the calculation of the flow exergy considering the physical and chemical exergies of the distillation process; the calculation of the primary and transformed exergy contributions considering the consumed exergy; and finally, the overall process efficiency, which shows the real percentage of energy being used in the process. The simulation of an extractive distillation separation system is carried out using Aspen Plus (R), from Aspen Tech Version 9. In general, heat transfer processes (heating or cooling) are the ones that generate the greatest exegetic destruction, which is why they must be the operations that must be optimized. As a result of our case study, the local exergy efficiency of the extractive distillation column is 13.80%, which is the operation with the greatest energy loss, and the overall exergy efficiency of the separation system is 30.67%. Then, in order to increase exergy efficiency, a sensitivity analysis is performed with the variation of the azeotrope feed, number of stages, reflux ratio, and solvent feed variation on ethanol purity to reach an overall efficiency of 33.53%. The purity of ethanol is classified as higher than that of the specified, 99.65%.
引用
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页数:14
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