Optimal Synthesis of Distillation Systems for Bioethanol Separation. Part 2. Extractive Distillation with Complex Columns

被引:49
作者
Errico, Massimiliano [1 ,2 ]
Rong, Ben-Guang [1 ]
Tola, Giuseppe [2 ]
Spano, Maurizio [2 ]
机构
[1] Univ So Denmark, Inst Chem Engn Biotechnol & Environm Technol, DK-5230 Odense M, Denmark
[2] Univ Cagliari, Dipartimento Ingn Meccan Chim & Mat, I-09123 Cagliari, Italy
关键词
DIVIDING-WALL COLUMNS; OPTIMIZATION; ENTRAINER; ETHANOL; DESIGN; DEHYDRATION; GLYCEROL; SCHEMES;
D O I
10.1021/ie301829n
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the first part of the work the dehydration of bioethanol by extractive distillation was considered to define the best simple column sequence. It was proved that among all the simple configurations generated, two sequences with three columns are able to consistently reduce the energy demand and the capital costs compare to the four-column sequence used as a reference. Then, starting from the selected simple column configurations different complex sequences were predicted. It was evidenced that thermally coupled configurations realized only a limited saving in the capital costs. The two column configuration with a vapor side stream is able to reduce the capital costs, but not all the solvent can be recovered. Its convenience is related to the trade-off between the solvent cost and the savings in the capital costs achieved. The two-column configurations with a divided wall column represent an excellent alternative for bioethanol production because their performances are not limited by the solvent recovery.
引用
收藏
页码:1620 / 1626
页数:7
相关论文
共 20 条
[1]   Dehydration of Bioethanol by Hybrid Process Liquid-Liquid Extraction/Extractive Distillation [J].
Aviles Martinez, Adriana ;
Saucedo-Luna, Jaime ;
Gabriel Segovia-Hernandez, Juan ;
Hernandez, Salvador ;
Israel Gomez-Castro, Fernando ;
Jaime Castro-Montoya, Agustin .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (17) :5847-5855
[2]   Design and optimization of thermally coupled distillation schemes for the separation of multicomponent mixtures [J].
Calzon-McConville, CJ ;
Rosales-Zamora, MB ;
Segovia-Hernández, JG ;
Hernández, S ;
Rico-Ramírez, V .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (02) :724-732
[3]  
Christiansen AC, 1997, COMPUT CHEM ENG, V21, pS237, DOI 10.1016/S0098-1354(97)87508-4
[4]   Process intensification for the retrofit of a multicomponent distillation plant - An industrial case study [J].
Errico, Massimiliano ;
Rong, Ben-Guang ;
Tola, Giuseppe ;
Turunen, Ilkka .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (06) :1975-1980
[5]   Optimal Synthesis of Distillation Systems for Bioethanol Separation. Part 1: Extractive Distillation with Simple Columns [J].
Errico, Massimiliano ;
Rong, Ben-Guang ;
Tola, Giuseppe ;
Spano, Maurizio .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (04) :1612-1619
[6]   Synthesis of new separation processes for bioethanol production by extractive distillation [J].
Errico, Massimiliano ;
Rong, Ben-Guang .
SEPARATION AND PURIFICATION TECHNOLOGY, 2012, 96 :58-67
[7]   A method for systematic synthesis of multicomponent distillation systems with less than N-1 columns [J].
Errico, Massimiliano ;
Rong, Ben-Guang ;
Tola, Giuseppe ;
Turunen, Ilkka .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2009, 48 (04) :907-920
[8]   Optimization of the Design and Operation of an Extractive Distillation System for the Production of Fuel Grade Ethanol Using Glycerol as Entrainer [J].
Garcia-Herreros, Pablo ;
Gomez, Jorge M. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (07) :3977-3985
[9]   Separation of ethanol and water by extractive distillation with salt and solvent as entrainer:: Process simulation [J].
Gil, I. D. ;
Uyazan, A. M. ;
Aguilar, J. L. ;
Rodriguez, G. ;
Caicedo, L. A. .
BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, 2008, 25 (01) :207-215
[10]   Control of an extractive distillation process to dehydrate ethanol using glycerol as entrainer [J].
Gil, Ivan D. ;
Gomez, Jorge M. ;
Rodriguez, Gerardo .
COMPUTERS & CHEMICAL ENGINEERING, 2012, 39 :129-142