Purification of xylanase from Bacillus pumilus using Eudragit S-100 and optimization of conditions

R. Kapilan, Vasanthy Arasaratnan
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Abstract

Soluble-insoluble polymers have considerable applications in the enzyme purification and these polymers precipitate from the solution by changing the pH. Eudragit S-100, nontoxic polymer of methacrylic acid and methyl methacrylate, has been used in affinity precipitation. The study describes the purification of xylanase from Bacillus pumilus by three phase partitioning (TPP) method and precipitation (PT) method using Eudragit S-100 and to optimize these methods to improve the purification fold. In the TPP method, 14.6 U mL-1 of xylanase activity was obtained with a specific activity of 31.74 U mg protein-1. The recovery of the enzyme was 52.24 % with 1.79-fold purification. In the PT method, 15 U mL-1 of xylanase activity was obtained with the specific activity of 33.4 U mg protein-1. The recovery of the enzyme was 52.18% with 1.72-fold purification. Since there is no significant difference in the purification folds of both these methods and to improve the purification fold, the conditions of these methods were optimized. When different concentrations of (NH4)2SO4 were used, xylanase with significantly higher specific activity (33.74 U mg protein-1) was precipitated with 50% of (NH4)2SO4 saturation. Among the different Eudragit concentrations used, 40gL-1 Eudragit S-100 yielded significantly higher xylanase activity (18.9 UmL-1) than the other Eudragit concentrations. When the spent medium was treated with 40gL-1 Eudragit S-100 and Eudragit bound xylanase was eluted with different concentrations of NaCl, significantly higher activity of xylanase (17.9UmL-1) was eluted with of 0.3 M NaCl. When TPP method of purification was done under optimized conditions (with 50% (NH4)2SO4 saturation and usage of 0.3 M NaCl for elution), 17.87U mL-1 of xylanase activity was obtained with a specific activity of 38.1 U mg protein-1and the xylanase enzyme yield and purification fold were significantly increased to 63.41% and 2.01 than the non-optimized TPP method. When PT method of purification was done under optimized conditions (with 40gL-1 Eudragit S-100 and usage of 0.3 M NaCl for elution), 18.96 U mL-1 of xylanase activity with the specific activity of 43.09 U mg protein-1 was obtained and the xylanase yield and the purification fold were significantly increased to 69.67% and 2.31 respectively than the non-optimized PT method. Since the purification fold of the optimized PT method is significantly higher than that of optimized TPP method, optimized PT method could be recommended for the purification of xylanase from Bacillus type bacteria. When the purified xylanase was subjected to poly acrylamide gel electrophoresis, it gave a single band and the molecular weight of the purified xylanase was determined as 55.4 kDa.
利用乌桕S-100纯化矮秆芽孢杆菌木聚糖酶及条件优化
可溶-不溶性聚合物在酶的纯化中有相当大的应用,这些聚合物通过改变ph从溶液中沉淀出来。Eudragit S-100是一种无毒的甲基丙烯酸和甲基丙烯酸甲酯聚合物,已被用于亲和沉淀。研究了以Eudragit S-100为原料,采用三相分割法(TPP)和沉淀法(PT)纯化短小芽孢杆菌中的木聚糖酶,并对这两种方法进行了优化,提高了纯化效率。TPP法获得的木聚糖酶活性为14.6 U mL-1,比活性为31.74 U mg protein-1。经1.79倍纯化,酶回收率为52.24%。PT法获得木聚糖酶活性为15 U mL-1,比活性为33.4 U mg protein-1。经1.72倍纯化,酶回收率为52.18%。由于两种方法的纯化倍数没有显著差异,为了提高纯化倍数,对两种方法的条件进行了优化。使用不同浓度的(NH4)2SO4时,在(NH4)2SO4饱和度为50%时,沉淀的木聚糖酶具有较高的比活性(33.74 U mg protein-1)。在不同浓度的木聚糖酶中,40gL-1木聚糖S-100的木聚糖酶活性显著高于其他浓度的木聚糖酶活性(18.9 μ l -1)。用40gL-1 Eudragit S-100处理废培养基,用不同浓度的NaCl洗脱Eudragit结合的木聚糖酶时,0.3 M NaCl洗脱的木聚糖酶活性显著提高(17.9 μ l -1)。在优化条件下(NH4 - 2SO4饱和度为50%,NaCl用量为0.3 M)进行TPP纯化,木聚糖酶活性为17.87U mL-1,比活性为38.1 U mg protein-1,木聚糖酶产率和纯化倍数较未优化的TPP显著提高,分别为63.41%和2.01倍。在优化条件下(40gL-1 Eudragit S-100, 0.3 M NaCl洗脱)进行PT法纯化,木聚糖酶活性为18.96 U mL-1,比活性为43.09 U mg protein-1,木聚糖酶产率和纯化倍数分别显著提高至69.67%和2.31%。由于优化后的PT法的纯化倍数明显高于优化后的TPP法,因此可以推荐优化后的PT法纯化芽孢杆菌型菌的木聚糖酶。纯化后的木聚糖酶经聚丙烯酰胺凝胶电泳显示为单带,纯化后的木聚糖酶分子量为55.4 kDa。
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