Direct extraction of phenylacetic acid from immobilised enzymatic hydrolysis of penicillin G with cloud point extraction

被引:13
作者
Wang, ZL [1 ]
Guo, YJ
Bao, D
Qi, HS
机构
[1] Shanghai Jiao Tong Univ, Sch Pharm, Shanghai 200240, Peoples R China
[2] Shanghai Highly Integrated Bioproc Sci & Technol, Shanghai 201101, Peoples R China
[3] Shanghai Jiao Tong Univ, Inst Biotechnol, Shanghai 200237, Peoples R China
关键词
penicillin acylase; hydrolysis; non-ionic surfactant; cloud point extraction;
D O I
10.1002/jctb.1479
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The enzymatic hydrolysis of potassium salt of penicillin G (Pen G) into phenylacetic acid (PAA) and potassium salt of 6-aminopenicillanic acid (APA) is inhibited not only by the substrate and the product APA but also by the by-product PAA. The partitioning behaviour of PAA in a cloud point system, a novel two-phase partitioning system, was determined. Direct extraction of PAA in the process of immobilised penicillin acylase hydrolysis of Pen G without pH control was achieved. Pen G was hydrolysed almost completely and the product APA concentration in the cloud point system was much higher than in the control, suggesting that the cloud point system may be applied as a novel extractive bioreactor for the enzymatic hydrolysis of Pen G. (c) 2006 Society of Chemical Industry.
引用
收藏
页码:560 / 565
页数:6
相关论文
共 26 条
[1]   Improving the industrial production of 6-APA:: Enzymatic hydrolysis of penicillin G in the presence of organic solvents [J].
Abian, O ;
Mateo, C ;
Fernández-Lorente, G ;
Guisán, JM ;
Fernández-Lafuente, R .
BIOTECHNOLOGY PROGRESS, 2003, 19 (06) :1639-1642
[2]  
Cao XJ, 2004, BIOTECHNOL LETT, V26, P97
[3]   Discrete countercurrent contacting: An experimental method for developing continuous countercurrent reactors [J].
den Hollander, JL ;
Aversente, A ;
Diender, MB ;
Straathof, AJJ ;
van der Wielen, LAM .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (01) :231-235
[4]   Continuous enzymatic penicillin G hydrolysis in countercurrent water-butyl acetate biphasic systems [J].
den Hollander, JL ;
Zomerdijk, M ;
Straathof, AJJ ;
van der Wielen, LAM .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (09) :1591-1598
[5]   Equilibrium modeling of extractive enzymatic hydrolysis of penicillin G with concomitant 6-aminopenicillanic acid crystallization [J].
Diender, MB ;
Straathof, AJJ ;
van der Does, T ;
Ras, C ;
Heijnen, JJ .
BIOTECHNOLOGY AND BIOENGINEERING, 2002, 78 (04) :395-402
[6]   Kinetic analysis of the effects of products removal on the hydrolysis of penicillin G by immobilised penicillin acylase [J].
Duan, G ;
Chen, JY .
PROCESS BIOCHEMISTRY, 1996, 31 (01) :27-30
[7]   Activity and stability of immobilized penicillin amidase at low pH values [J].
Ferreira, JS ;
Straathof, AJJ ;
Franco, TT ;
van der Wielen, LAM .
JOURNAL OF MOLECULAR CATALYSIS B-ENZYMATIC, 2004, 27 (01) :29-35
[8]   IN-SITU PRODUCT REMOVAL AS A TOOL FOR BIOPROCESSING [J].
FREEMAN, A ;
WOODLEY, JM ;
LILLY, MD .
BIO-TECHNOLOGY, 1993, 11 (09) :1007-1012
[9]   Intensification of enzymatic hydrolysis of penicillin G: Part 2. Model for enzymatic reaction with reactive extraction [J].
Gaidhani, HK ;
Tolani, VL ;
Pangarkar, KV ;
Pangarkar, VG .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (11) :1985-1992
[10]  
Gaidhani HK, 2002, CHEM ENG SCI, V57, P1979