摘要
以青霉素酰化酶基因重组大肠杆菌A56(pPA22),经戊二醛交联(防止细胞自溶)后,在PEG2000-DextranT70两水相体系中进行转化反应,生产6-氨基青霉烷酸(6-APA)。实现含酶菌体在两水相体系中的单侧分配。考察了菌体加量对青霉素转化率的影响。在两水相体系中进行5批半连续转化反应,底物浓度为7%,转化率在90%以上,反应时间为40分钟,比生产速率为3·6~4·6μmol/ml·min,下相酶活为52u/ml,并从上相中直接结晶6-APA,6-APA的纯度为96·2%。实现了高底物浓度,高转化率,缩短反应时间和产物不需浓缩直接结晶之目的。在两水相体系中生产6-APA成为又一新的青霉素酰化酶应用形式。
In this paper,Penicillin bioconversion in PEG20000-De- xtran T70 aqueous two-phase system has been studied.The bacterial part-itioning was totally biased to the bottom phase under suitable conditions.The optimum reaction conditions were found to be:7%(w/v)substrate(Penicillin G),enzyme activity in the bottom phase 52 u/ml, pH7.8,te-mperature 37℃,reaction time 40 min. Repeated batch conversion was ca-rried out four times by replacing the top phase at optimum condition. The average conversion ratio of Penicillin exceeded 90%。Specific produc-tivity based on the bottom phase was 3.6~4.6μmol/ml·min,The product,6-APA could directly be crystallized from top phase with a purity of 96.2%
出处
《中国抗生素杂志》
CAS
CSCD
北大核心
1994年第2期131-133,共3页
Chinese Journal of Antibiotics
关键词
生物转化
大肠杆菌
青霉素酰化酶
Bioconversion,Aqueous Two-phase Systems
6-APA
Penicillin G
Recombinant E.coli:Penicillin Acylase