Department of Food Science and Technology, School of Chemistry, Universidad Autonoma de Coahuila, ZIP 25280, Saltillo, Coahuila, Mexico.
J Microbiol Biotechnol. 2011 Sep;21(9):960-7.
Tannin acyl hydrolase, also known as tannase, is an enzyme with important applications in the food, feed, pharmaceutical, and chemical industries. However, despite a growing interest in the catalytic properties of tannase, its practical use is very limited owing to high production costs. Several studies have already demonstrated the advantages of solid-state fermentation (SSF) for the production of fungal tannase, yet the optimal conditions for enzyme production strongly depend on the microbial strain utilized. Therefore, the aim of this study was to improve the tannase production by a locally isolated A. niger strain in an SSF system. The SSF was carried out in packed-bed bioreactors using polyurethane foam as an inert support impregnated with defined culture media. The process parameters influencing the enzyme production were identified using a Plackett–Burman design, where the substrate concentration, initial pH, and incubation temperature were determined as the most significant. These parameters were then further optimized using a Box-Behnken design. The maximum tannase production was obtained with a high tannic acid concentration (50 g/l), relatively low incubation temperature (30°C), and unique low initial pH (4.0). The statistical strategy aided in increasing the enzyme activity nearly 1.97-fold, from 4,030 to 7,955 U/l. Consequently, these findings can lead to the development of a fermentation system that is able to produce large amounts of tannase in economical, compact, and scalable reactors.
单宁酰基水解酶,也被称为单宁酶,是一种在食品、饲料、制药和化学工业中具有重要应用的酶。然而,尽管人们对单宁酶的催化特性越来越感兴趣,但由于生产成本高,其实际应用非常有限。已有多项研究表明固态发酵(SSF)在真菌单宁酶生产中的优势,但酶生产的最佳条件强烈依赖于所使用的微生物菌株。因此,本研究旨在通过固态发酵系统提高本地分离的黑曲霉菌株的单宁酶产量。SSF 在填充床生物反应器中进行,使用聚氨酯泡沫作为惰性载体,浸渍有定义的培养基。使用 Plackett–Burman 设计确定了影响酶生产的过程参数,其中底物浓度、初始 pH 和培养温度被确定为最重要的参数。然后使用 Box-Behnken 设计进一步优化这些参数。在高单宁酸浓度(50 g/l)、相对较低的培养温度(30°C)和独特的低初始 pH(4.0)下,获得了最大的单宁酶产量。统计策略有助于将酶活性从 4,030 提高到 7,955 U/l,几乎提高了 1.97 倍。因此,这些发现可以为开发能够在经济、紧凑和可扩展的反应器中大量生产单宁酶的发酵系统提供依据。