Stark D, Kornmann H, Münch T, Sonnleitner B, Marison I W, von Stockar U
Laboratory of Chemical and Biochemical Engineering, Swiss Federal Institute of Technology (EPFL), CH-1015 Lausanne, Switzerland.
Biotechnol Bioeng. 2003 Aug 20;83(4):376-85. doi: 10.1002/bit.10679.
A novel in situ product removal (ISPR) method that uses microcapsules to extract inhibitory products from the reaction suspension is introduced into fermentation technology. More specifically, L-phenylalanine (L-Phe) was transformed by Saccharomyces cerevisiae to 2-phenylethanol (PEA), which is inhibitory toward the yeast. In order to continuously remove PEA from the vicinity of the cells, the reaction suspension was brought into contact with capsules of 2.2-mm diameter that had a hydrophobic core of dibutyl sebacate and an alginate-based wall. This novel process combines the advantages of a normal in situ extraction process (fast mass transfer and simple process set-up) with the benefits of a membrane-based process (reduction of the solvent toxicity and avoidance of stable emulsions). In particular, the microbial cells are shielded from the phase toxicity of the organic solvent by a hydrogel layer surrounding the organic core. By placing the microcapsules into the fermenter, the final overall concentration of PEA in a fed-batch culture was increased from 3.8 to 5.6 g/L because a part of the inhibitory product dissolved in the dibutyl sebacate core. In another fermentation experiment, the capsules were placed in a fluidized bed that was connected via a loop to the fermenter. In addition, the fluidized bed was connected via a second loop to a back-extractor to regenerate the capsules. By alternating the extraction and back-extraction cycles, it was possible to limit the PEA concentration of the fed-batch culture in the fermenter to 2.4 g/L while producing important quantities of PEA that accumulated in an external reservoir.
一种利用微胶囊从反应悬浮液中提取抑制性产物的新型原位产物去除(ISPR)方法被引入发酵技术。更具体地说,酿酒酵母将L-苯丙氨酸(L-Phe)转化为对酵母有抑制作用的2-苯乙醇(PEA)。为了从细胞附近连续去除PEA,使反应悬浮液与直径为2.2毫米的胶囊接触,这些胶囊具有癸二酸二丁酯疏水核心和藻酸盐基壁。这种新工艺结合了常规原位萃取工艺的优点(传质快且工艺设置简单)和基于膜的工艺的优点(降低溶剂毒性并避免形成稳定乳液)。特别是,微生物细胞被围绕有机核心的水凝胶层与有机溶剂的相毒性隔离开来。通过将微胶囊放入发酵罐中,补料分批培养中PEA的最终总浓度从3.8克/升提高到5.6克/升,因为一部分抑制性产物溶解在癸二酸二丁酯核心中。在另一个发酵实验中,将胶囊置于通过回路连接到发酵罐的流化床中。此外,流化床通过第二个回路连接到反萃取器以再生胶囊。通过交替进行萃取和反萃取循环,可以将发酵罐中补料分批培养的PEA浓度限制在2.4克/升,同时产生大量积累在外部储存器中的PEA。