PARTITION BEHAVIOR AND PURIFICATION OF A MUCOR-BACILLIFORMIS ACID PROTEASE IN AQUEOUS 2-PHASE SYSTEMS

被引:24
作者
LAHORE, HMF [1 ]
MIRANDA, MV [1 ]
FRAILE, ER [1 ]
BONINO, MJBD [1 ]
CASCONE, O [1 ]
机构
[1] UNIV BUENOS AIRES, CONICET, IQUIFIB, RA-1113 BUENOS AIRES, DF, ARGENTINA
关键词
D O I
10.1016/0032-9592(94)00026-3
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
The partitioning of a Mucor bacilliformis acid protease, a potential substitute for bovine chymosin in cheese manufacture, was accomplished in various aqueous two-phase systems in order to investigate how changes in factors such as PEG (poly(ethylene glycol)) molecular weight, pH and sodium chloride concentration, can modify the partition coefficient value. PEG-Reppal and PEG-phosphate systems were evaluated, in the presence of contaminating material from the solid substrate fermentation of the microorganism. When PEG-phosphate systems were analysed it was found that K-AP depended strongly on the PEG molecular weight (at pH 5.0, an increase in PEG molecular weight from 600 to 20000 leads to a decrease in the K value from > 50 to 0.1). A dependence between K-AP and system pH was also noticed, this effect being important at lower/intermediate PEG molecular weight. When PEG 1540 was used a V-shaped distribution of K-AP, values was obtained, with a minimum at pH 5.0 (K = 1.40) and maxima at pH values of 3.0 (K> 40) and 5.8 (K = 14). Furthermore, the addition of NaCl led to an increase in K-AP (for PEG 3350/phosphate at pH 5.0, K increased from 1.1 to > 35 when 1.0 mol kg(-1) NaCl was added). Suitable conditions for enzyme purification were found in PEG 3350-phosphate systems at pH 3.0 and NaCl 1.0 mol kg(-1) (K-AP > 35, K-CP = 0.10) and PEG-Reppal at pH 3.0, NaCl 1.5 mol kg(-1) (K-AP = 13, K-CP = 0.32). In these systems, proteinaceous and particulate contaminating materials precipitated and adsorbed at the interphase, thus yielding a clear upper phase containing the purified enzyme. Furthermore, direct extraction of the fermented mass was peformed using a PEG 20 000-Reppal-NaCl system (K-AP = 14, K-CP = 0.19, PF (purification factor) = 5.9). The enzyme can be recovered in the PEG 20 000-rich phase and back-extracted by adding salt (K-AP = 0.25, K-CP = 1.10, PF = 1.7). This method provides a simpler process for leaching and purification of an enzyme produced by solid-state fermentation.
引用
收藏
页码:615 / 621
页数:7
相关论文
共 22 条
[1]  
Abbott N L, 1990, Bioseparation, V1, P191
[2]  
Albertsson P., 1986, PARTITION CELL PARTI
[3]  
Albertsson P. A., 1990, SEPARATION PROCESSES, P287
[4]   PURIFICATION AND CHARACTERIZATION OF A MILK CLOTTING PROTEASE FROM MUCOR-BACILLIFORMIS [J].
ARECES, LB ;
BONINO, MBD ;
PARRY, MAA ;
FRAILE, ER ;
FERNANDEZ, HM ;
CASCONE, O .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 1992, 37 (03) :283-294
[5]  
Arima K., 1970, METHODS ENZYMOLOGY, V19, P446, DOI 10.1016/0076-6879(70)19033-1
[6]  
BRADFORD MM, 1976, ANAL BIOCHEM, V72, P248, DOI 10.1016/0003-2697(76)90527-3
[7]  
CARLSON A, 1988, SEP SCI TECHNOL, V23, P765
[8]   PARTITIONING AND PURIFICATION OF THAUMATIN IN AQUEOUS 2-PHASE SYSTEMS [J].
CASCONE, O ;
ANDREWS, BA ;
ASENJO, JA .
ENZYME AND MICROBIAL TECHNOLOGY, 1991, 13 (08) :629-635
[9]  
CHEN J-P, 1987, Biotechnology Techniques, V1, P263, DOI 10.1007/BF00155466
[10]  
DOVE GB, 1986, SEPARATION RECOVERY, V314, P93