Optimal Synthesis of Distillation Systems for Bioethanol Separation. Part 1: Extractive Distillation with Simple Columns

被引:61
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
HOMOGENEOUS AZEOTROPIC DISTILLATION; ETHANOL DEHYDRATION; DESIGN; TECHNOLOGIES; SIMULATION; OPERATION; SEQUENCES; STRATEGY;
D O I
10.1021/ie301828d
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The article presents an analysis between different possible sequences for the separation of bioethanol from a typical fermentor's stream. The preconcentrator column, necessary to approach the azeotropic composition was included as a fundamental part of the sequences. Starting from a recently proposed four-column configuration in the literature, a full set of alternatives was predicted and explored in detail. Different combinations of partial and total condensers were considered so as to possibly reduce the amount of equipment. 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. The results obtained represent the first step for the further generation of complex configuration sequences.
引用
收藏
页码:1612 / 1619
页数:8
相关论文
共 48 条
[1]   Synthesis of multicomponent distillation column configurations [J].
Agrawal, R .
AICHE JOURNAL, 2003, 49 (02) :379-401
[2]  
Al-Hasan A, 2003, ENERG CONVERS MANAGE, V44, P1547
[3]  
[Anonymous], 1997, PERRYS CHEM ENG HDB
[4]   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
[5]   Design of distillation sequences: from conventional to fully thermally coupled distillation systems [J].
Caballero, JA ;
Grossmann, IE .
COMPUTERS & CHEMICAL ENGINEERING, 2004, 28 (11) :2307-2329
[6]   ETHANOL DEHYDRATION BY AZEOTROPIC DISTILLATION WITH A MIXED-SOLVENT ENTRAINER [J].
CHIANESE, A ;
ZINNAMOSCA, F .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1990, 43 (02) :59-65
[7]   DESIGN AND SYNTHESIS OF HOMOGENEOUS AZEOTROPIC DISTILLATIONS .3. THE SEQUENCING OF COLUMNS FOR AZEOTROPIC AND EXTRACTIVE DISTILLATIONS [J].
DOHERTY, MF ;
CALDAROLA, GA .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1985, 24 (04) :474-485
[8]   A MIXED-INTEGER NONLINEAR-PROGRAMMING ALGORITHM FOR PROCESS SYSTEMS SYNTHESIS [J].
DURAN, MA ;
GROSSMANN, IE .
AICHE JOURNAL, 1986, 32 (04) :592-606
[9]   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
[10]   Modeling, simulation and control of an internally heat integrated pressure-swing distillation process for bioethanol separation [J].
Francisco Mulia-Soto, Jorge ;
Flores-Tlacuahuac, Antonio .
COMPUTERS & CHEMICAL ENGINEERING, 2011, 35 (08) :1532-1546