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Modelling and Intensification of Biocatalytic Production of Natural Compounds Performed in Hybrid Systems

机译:杂交系统中生物催化生物催化生物催化的建模与强化

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In the past two decades, continuous growth of natural compounds production by biocatalytic conversion of different substrates can be observed. Biocatalytic production of many natural compounds is usually connected with a strong inhibition effect of the product. Therefore, strong academic and industrial interest has been devoted to the integration of reaction and separation steps into one operation unit, which can save raw materials, increase the productivity of the process and save capital and operational costs. In this paper, possibilities of biotechnological production of natural aroma 2-phenylethanol in different hybrid systems are discussed and compared with classical batch fermentation. Hybrid systems with in situ removal of the product from the fermentation broth are based on a combination of a bioreactor with membrane units like microfiltration, membrane based solvent extraction and a distillation unit. Two different configurations of hybrid systems were compared with the classical batch technology. The application of verified mathematical models of operational units (bioreactor, microfiltration module, extraction module, distillation unit) has shown, that the hybrid system, where the membrane module for extraction is immersed directly in the bioreactor can increase the annual productivity by approximately 1.7 times.
机译:在过去二十年中,可以观察到通过不同底物的生物催化转化产生的天然化合物的持续生长。许多天然化合物的生物催化作用通常与产品的强抑制效果相连。因此,强有力的学术和工业利益致力于将反应和分离步骤的整合到一个操作单元中,这可以节省原材料,提高过程的生产率,并节省资本和运营成本。本文讨论了不同杂合系统中天然香气2-苯基乙醇的生物技术生产的可能性,并与经典分批发酵进行比较。具有原位除去来自发酵液的产物的杂化系统基于生物反应器的组合,所述生物反应器具有膜单元,如微滤,基于膜溶剂萃取和蒸馏装置。将两种不同的混合系统配置与典型批量技术进行了比较。验证的操作单元数学模型(生物反应器,微滤模块,提取模块,蒸馏装置)所示,其中杂交系统,其中萃取膜模块直接浸入生物反应器中,可以将年生产率提高约1.7倍。

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