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Improved Production and In Situ Recovery of Sesquiterpene (+)-Zizaene from Metabolically-Engineered E. coli

机译:从代谢工程大肠杆菌中提高倍半萜烯(+)-紫氮烯的生产和原位回收

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摘要

The sesquiterpene (+)-zizaene is the direct precursor of khusimol, the main fragrant compound of the vetiver essential oil from Chrysopogon zizanioides and used in nearly 20% of men’s fine perfumery. The biotechnological production of such fragrant sesquiterpenes is a promising alternative towards sustainability; nevertheless, product recovery from fermentation is one of the main constraints. In an effort to improve the (+)-zizaene recovery from a metabolically-engineered Escherichia coli, we developed an integrated bioprocess by coupling fermentation and (+)-zizaene recovery using adsorber extractants. Initially, (+)-zizaene volatilization was confirmed from cultivations with no extractants but application of liquid–liquid phase partitioning cultivation (LLPPC) improved (+)-zizaene recovery nearly 4-fold. Furthermore, solid–liquid phase partitioning cultivation (SLPPC) was evaluated by screening polymeric adsorbers, where Diaion HP20 reached the highest recovery. Bioprocess was scaled up to 2 L bioreactors and in situ recovery configurations integrated to fermentation were evaluated. External recovery configuration was performed with an expanded bed adsorption column and improved (+)-zizaene titers 2.5-fold higher than LLPPC. Moreover, internal recovery configuration (IRC) further enhanced the (+)-zizaene titers 2.2-fold, whereas adsorption velocity was determined as critical parameter for recovery efficiency. Consequently, IRC improved the (+)-zizaene titer 8.4-fold and productivity 3-fold from our last report, achieving a (+)-zizaene titer of 211.13 mg L−1 and productivity of 3.2 mg L−1 h−1. This study provides further knowledge for integration of terpene bioprocesses by in situ product recovery, which could be applied for many terpene studies towards the industrialization of fragrant molecules.
机译:倍半萜烯(+)-zi嗪烯是苦瓜酚的直接前体,苦瓜酚是香茅(Chrysopogon zizanioides)香根草精油的主要香气成分,在将近20%的男性高级香水中使用。这种芳香倍半萜的生物技术生产是可持续发展的有前途的替代方法。然而,从发酵中回收产物是主要限制之一。为了改善从代谢工程化的大肠杆菌中回收(+)-za烯的方法,我们开发了一种结合发酵过程和使用吸附剂萃取剂回收(+)-zi烯的生物工艺。最初,在没有萃取剂的情况下证实了(+)-za烯挥发,但是应用液相-液相分配培养(LLPPC)可以使(+)-烯的回收率提高近4倍。此外,通过筛选聚合物吸附器评估了固液相分配培养(SLPPC),其中Diaion HP20的回收率最高。将生物工艺放大至2 L生物反应器,并评估整合到发酵中的原位回收配置。外部回收配置是使用扩展床吸附柱进行的,并且改进的(+)-za氮效价比LLPPC高2.5倍。此外,内部回收构型(IRC)进一步提高了(+)-zi烯效价2.2倍,而吸附速度被确定为回收效率的关键参数。因此,IRC将我们的上一份报告中的(+)-zi嗪效价提高了8.4倍,将生产率提高了3倍,实现了(+)-zane效价为211.13 mg L -1 和3.2 mg L -1 h -1 。这项研究为通过原位产物回收整合萜烯生物过程提供了进一步的知识,可将其应用于许多萜烯研究,以实现芳香分子的工业化。

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