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从发酵液中纯化2,3-丁二醇:工艺开发与技术经济分析

Purification of 2,3-butanediol from fermentation broth: process development and techno-economic analysis.

作者信息

Harvianto Gregorius Rionugroho, Haider Junaid, Hong Jimin, Van Duc Long Nguyen, Shim Jae-Jin, Cho Moo Hwan, Kim Woo Kyoung, Lee Moonyong

机构信息

School of Chemical Engineering, Yeungnam University, Dae-dong 214-1, Gyeongsan, 38541 Republic of Korea.

出版信息

Biotechnol Biofuels. 2018 Jan 25;11:18. doi: 10.1186/s13068-018-1013-3. eCollection 2018.

Abstract

BACKGROUND

2,3-Butanediol (2,3-BDO) is a synthetic chemical compound that also can be produced by biomass fermentation, which is gaining share in the global market as an intermediate product for numerous applications, i.e. as liquid fuel or fuel additive. Several metabolic engineering fermentation strategies to enhance the production of 2,3-BDO were developed. However, the recovery of 2,3-BDO from its fermentation broth remains a challenge due to its low concentration and its solubility in water and other components. Thus, a cost-effective recovery process is required to deliver the required purity of 2,3-BDO. This paper presents a new process development and techno-economic analysis for 2,3-BDO purification from a fermentation broth.

RESULTS

Conventional distillation and hybrid extraction-distillation (HED) processes are proposed in this study with detailed optimization and economic analysis. Particularly, a systematic solvent selection method was successfully implemented to determine a good solvent for the proposed HED configuration based on numerous experimental data obtained with each solvent candidate. NRTL and UNIQUAC property methods were evaluated to obtain binary interaction parameters of 2,3-BDO through rigorous Aspen Plus regression and validated using experimental data. Total annual cost (TAC)-based optimization was performed for each proposed configuration. Even though the HED configuration required 9.5% higher capital cost than conventional distillation, placing an extraction column before the distillation column was effective in removing water from the fermentation broth and significantly improved the overall process economics.

CONCLUSIONS

Oleyl alcohol was found to be the most suitable solvent for the HED of 2,3-BDO due to its high distribution coefficient and high selectivity. The proposed HED drastically reduced reboiler duty consumption and TAC by up to 54.8 and 25.8%, respectively. The proposed design is expected to be used for the commercial scale of 2,3-BDO production from fermentation process.

摘要

背景

2,3-丁二醇(2,3-BDO)是一种合成化合物,也可通过生物质发酵生产,作为多种应用的中间产品,它在全球市场中的份额不断增加,例如用作液体燃料或燃料添加剂。已开发出多种代谢工程发酵策略来提高2,3-丁二醇的产量。然而,由于2,3-丁二醇在发酵液中的浓度较低且可溶于水和其他成分,从发酵液中回收2,3-丁二醇仍然是一项挑战。因此,需要一种经济高效的回收工艺来提供所需纯度的2,3-丁二醇。本文介绍了一种从发酵液中纯化2,3-丁二醇的新工艺开发和技术经济分析。

结果

本研究提出了常规蒸馏和萃取-蒸馏混合(HED)工艺,并进行了详细的优化和经济分析。特别是,基于从每个候选溶剂获得的大量实验数据,成功实施了一种系统的溶剂选择方法,以确定适合所提出的HED配置的良好溶剂。通过严格的Aspen Plus回归评估了NRTL和UNIQUAC物性方法,以获得2,3-丁二醇的二元相互作用参数,并使用实验数据进行了验证。对每个提出的配置进行了基于年度总成本(TAC)的优化。尽管HED配置的资本成本比常规蒸馏高9.5%,但在蒸馏塔之前设置萃取塔可有效去除发酵液中的水,并显著改善了整体工艺经济性。

结论

由于油醇具有较高的分配系数和选择性,因此被发现是2,3-丁二醇HED最适合的溶剂。所提出的HED分别使再沸器热负荷消耗和TAC大幅降低了54.8%和25.8%。预计所提出的设计将用于发酵法生产2,3-丁二醇的商业规模。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/8708/5785907/d63504dec874/13068_2018_1013_Fig1_HTML.jpg

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