生物转化后回收2-苯乙醇和2-苯乙酸乙酯的先进下游工艺设计

IF 2.4 4区 生物学 Q3 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
Tamara Janković, Adrie JJ Straathof, Anton A Kiss
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引用次数: 0

摘要

背景2-苯乙醇(2-PE)和2-苯乙酸乙酯(2-PEAc)是有价值的芳香化合物,市场需求不断增长。作为传统石油化工生产的替代品,生物转化可以获得更有价值的这些化学物质的自然形式。由于产品对微生物具有显著的毒性,产品的低浓度和产品的高沸点使回收过程复杂化。通过液-液萃取的原位产品回收可用于提高生物工艺收率和生产率。然而,由于2-PE和2-PEAc的多相、主要产物的高沸点温度、剩余底物和副产物的存在以及微生物的存在,2-PE和2-PEAc的后续纯化具有挑战性。结果本研究的主要目的是利用硅法开发一种先进的工业工艺,用于离心后的最终纯化,以提高2-PE生物技术生产的竞争力。设计了一种适应性隔板柱,用于从有机相中去除含2-PEAc的2-PE或将2-PE酯化为纯2-PEAc。开发过程的生产灵活性允许根据市场需求进行调整。此外,从水相中回收联合生产的乙醇可以提高所开发工艺的经济和环境性能。详细的技术经济分析证实,该工艺具有成本效益(总回收成本为0.64-0.72美元/kg2-PE/2-PEAc)和能源效率(一次能源需求为1.83-2.05 kWthh/kg2-PE/2-PEAc),可回收生物转化后的2-PE或2-PEAc。结论所开发的工艺通过降低成本和能源需求,提高了生物技术2-PE生产的经济和环境可行性,同时保证了适应市场需求的灵活性。©2025作者。由John Wiley &; Sons Ltd代表美国化学工业学会(SCI)出版的化学技术与生物技术杂志。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Advanced downstream process design for recovery of 2-phenylethanol and 2-phenylethyl acetate after biotransformation

Advanced downstream process design for recovery of 2-phenylethanol and 2-phenylethyl acetate after biotransformation

Advanced downstream process design for recovery of 2-phenylethanol and 2-phenylethyl acetate after biotransformation

Advanced downstream process design for recovery of 2-phenylethanol and 2-phenylethyl acetate after biotransformation

BACKGROUND

2-Phenylethanol (2-PE) and 2-phenylethyl acetate (2-PEAc) are valuable aroma compounds with growing market demands. As an alternative to conventional petrochemical production, more valuable natural forms of these chemicals can be obtained by biotransformation. Low product concentrations, resulting from significant product toxicity to microorganisms, and high boiling points of products complicate recovery process. In situ product recovery by liquid–liquid extraction can be used to increase bioprocess yield and productivity. However, the subsequent purification of 2-PE and 2-PEAc is challenging as a consequence of the multiple phases, high-boiling temperatures of main products, occurrence of remaining substrate and byproducts, and presence of microorganisms.

RESULTS

The main goal of this original work is to improve the competitiveness of the biotechnological production of 2-PE by using in silico methods to develop an advanced industrial process for the final purification after centrifugation. An adaptable dividing-wall column was designed to remove 2-PE with 2-PEAc from organic phase or to esterify 2-PE to pure 2-PEAc. The production flexibility of the developed process allows adjustability to market demand. Additionally, recovery of co-produced ethanol from aqueous phase can increase the economic and environmental performance of the developed process. As confirmed by detailed techno-economic analysis, the proposed processes can cost-effectively (total recovery costs of 0.64–0.72 US$/kg2-PE/2-PEAc) and energy-efficiently (primary energy requirements of 1.83–2.05 kWthh/kg2-PE/2-PEAc) recovery of 2-PE or 2-PEAc after biotransformation.

CONCLUSION

The developed process enhances economic and environmental viability of biotechnological 2-PE production by reducing costs and energy requirements, while ensuring flexibility to adapt to market demands. © 2025 The Author(s). Journal of Chemical Technology and Biotechnology published by John Wiley & Sons Ltd on behalf of Society of Chemical Industry (SCI).

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来源期刊
CiteScore
7.00
自引率
5.90%
发文量
268
审稿时长
1.7 months
期刊介绍: Journal of Chemical Technology and Biotechnology(JCTB) is an international, inter-disciplinary peer-reviewed journal concerned with the application of scientific discoveries and advancements in chemical and biological technology that aim towards economically and environmentally sustainable industrial processes.
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