Continuous predispersed solvent extraction process for the downstream separation of 2,3-butanediol from fermentation broth

被引:14
作者
Birajdar, Snehal D. [1 ,2 ]
Rajagopalan, Srinivasan [1 ,2 ]
Sawant, Jayant S. [1 ,2 ]
Padmanabhan, Sasisanker [2 ]
机构
[1] Savitribai Phule Pune Univ, Dept Technol, Pune, Maharashtra, India
[2] Div Praj Ind Ltd, Praj Matrix R&D Ctr, Pune, Maharashtra, India
关键词
2,3-Butanediol; Solvent extraction; Colloidal liquid aphrons; Bubble column; Mass transfer characteristics; COLLOIDAL LIQUID APHRONS; MASS-TRANSFER; EQUILIBRIUM; STABILITY; REMOVAL; ACID; RECOVERY;
D O I
10.1016/j.seppur.2015.07.037
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
2,3-Butanediol (BDO) offers the possibility of expanding the list of value-added chemicals produced from the biorefinery platform. However, a major challenge and technical bottleneck for an efficient biological production in a large scale is the separation of BDO from the fermented broth system. The use of colloidal liquid aphrons (CLAs) in pre-dispersed solvent extraction (PDSE) is considered as an emerging technique for the recovery of bio-based compounds. Herein, we describe the application of an environment friendly PDSE system using CLAs for the recovery of (BDO). Continuous mode of countercurrent extraction employing CLAs is demonstrated for the extraction of synthetic as well as fermented BDO in a bubble column apparatus. For the first time, the use of centrifugal contactor (CCS) is established for the formation of stable CLAs. The optimum system parameters required for the CLA formation using CCS method were: 0.25 wt% sodium dodecyl sulfate (SDS) as ionic surfactant, 0.5 wt% Tween 80 as non-ionic surfactant in butanol-water system having a flow ratio of 2 with agitation of 2000 rpm. Compared to the traditional liquid-liquid extraction (LLE) process, PDSE method provided 35-85% increase in mass transfer coefficient and about 30% reduction in overall solvent loading. In the presence of CLA.s, the distribution coefficient (K-d) of BDO was found to be similar for all the concentrations of BDO. The results of this work open up the scope of PDSE-CLAs for the downstream processing of other biorefinery products. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:115 / 123
页数:9
相关论文
共 47 条
[1]  
[Anonymous], Perry's chemical engineers' handbook
[2]  
[Anonymous], CATAL GROUP RESOUR
[3]  
[Anonymous], INT J CHEM ENG APPL
[4]  
[Anonymous], LIQUID LIQUID EXTRAC
[5]   Rapid Solvent Screening Using Thermodynamic Models for Recovery of 2,3-Butanediol from Fermentation by Liquid-Liquid Extraction [J].
Birajdar, Snehal D. ;
Padmanabhan, Sasisanker ;
Rajagopalan, Srinivasan .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2014, 59 (08) :2456-2463
[6]   Production of 2,3-butanediol from pretreated corn cob by Klebsiella oxytoca in the presence of fungal cellulase [J].
Cao, NJ ;
Xia, YK ;
Gong, CS ;
Tsao, GT .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 1997, 63-5 (1) :129-139
[7]   Biotechnological production of 2,3-butanediol-Current state and prospects [J].
Celinska, E. ;
Grajek, W. .
BIOTECHNOLOGY ADVANCES, 2009, 27 (06) :715-725
[8]   Improved 2,3-butanediol production from corncob acid hydrolysate by fed-batch fermentation using Klebsiella oxytoca [J].
Cheng, Ke-Ke ;
Liu, Qing ;
Zhang, Jian-An ;
Li, Jin-Ping ;
Xu, Jing-Ming ;
Wang, Ge-Hua .
PROCESS BIOCHEMISTRY, 2010, 45 (04) :613-616
[9]  
DECKWER WD, 1974, CHEM ENG SCI, V29, P2177, DOI 10.1016/0009-2509(74)80025-4
[10]  
Deshmukh AN, 2015, INT J ADV BIOTECHNOL, V6, P66