Dynamics of continuous flash fermentation for butanol production

被引：9
|
作者：
Mariano, Adriano Pinto [1 ]
Borba Costa, Caliane Bastos [1 ]
de Angelis, Dejanira de Franceschi [2 ]
Maugeri Filho, Francisco [3 ]
Pires Atala, Daniel Ibraim [3 ]
Wolf Maciel, Maria Regina [1 ]
Maciel Filho, Rubens [1 ]
机构：
[1] Univ Campinas UNICAMP, Sch Chem Engn, POB 6066, BR-13083970 Campinas, SP, Brazil
[2] Univ Estadual Paulista, Sao Paulo State Univ, Inst Biosci, Dept Biochem & Microbiol, Sao Paulo, SP, Brazil
[3] Univ Campinas UNICAMP, Sch Food Engn, Campinas, SP, Brazil
来源：
IBIC2010: 2ND INTERNATIONAL CONFERENCE ON INDUSTRIAL BIOTECHNOLOGY | 2010年 / 20卷
基金：
巴西圣保罗研究基金会;
关键词：
D O I：
10.3303/CET1020048
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
The ABE (acetone, butanol, ethanol) fermentation is characterized by its low productivity. In this paper, this issue is overcome with an innovative industrial process that employs the flash fermentation technology. The process consists of three interconnected units, as follows: fermentor, cell retention system (tangential microfiltration) and vacuum flash vessel (responsible for the continuous recovery of butanol from the broth). The dynamic behaviour of the process is described by a non-linear mathematical model with kinetic parameters determined experimentally. From simulations of the mathematical model the dynamic characteristic of the process were investigated. Analyzes of the open-loop dynamic behavior of the process, after step perturbations in the manipulated variables, determined the best control structures for the process.
引用
收藏
页码：285 / 290
页数：6
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