地中海Haloferax生产PHBV中挥发性脂肪酸的产酸发酵研究

Leire Urbina, Eric Rovira-Cal, Ibai Nafarrate, Ana Urkiaga, Josu Berganza, Enrique Aymerich and Maria José Suárez
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引用次数: 0

摘要

本研究对奶酪乳清(CW)进行了产酸发酵(AF),以获得不同挥发性脂肪酸(VFA)谱的流,用于聚羟基烷酸酯(PHA)的生物合成。在中温和亲热条件下,在单相反应器中进行了参数优化,得到了VFA含量为2718.2 mg L−1(乙酸为主,1288 mg L−1,丙酸为主,1119 mg L−1)和2270.2 mg L−1(丁酸为主,1339 mg L−1)的液流。在两相渗滤液床反应器中扩大了嗜热条件,得到了VFA浓度为7879 mg L−1的最终流,主要由丁酸组成。然后,验证了将所得液作为底物以地中海卤黄生产聚(3-羟基丁酸酯-共戊酸酯)(PHBV)的技术可行性。PHBV的产量与丁酸含量有关,当使用富含丁酸和丙酸的流时,PHBV的产量分别为1.4 g L−1和0.3 g L−1,但单体组成取决于丙酸的存在。在生物反应器条件下培养120 h后,PHVB产量达到2.43 g L−1,PHA积累达到44.3%。将生产的PHBV生物塑料与商品级PHA的特性进行了比较,发现两者相似。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Acidogenic fermentation of dairy by-products for the utilization of volatile fatty acids IN PHBV production by Haloferax mediterranei†

Acidogenic fermentation of dairy by-products for the utilization of volatile fatty acids IN PHBV production by Haloferax mediterranei†

In this study, the acidogenic fermentation (AF) of cheese whey (CW) has been conducted to obtain streams with different volatile fatty acid (VFA) profiles for polyhydroxyalkanoate (PHA) biosynthesis. AF was carried out in single-phase reactors for parameter optimization under mesophilic and thermophilic conditions, and streams with 2718.2 mg L−1 of VFA (predominantly acetic acid, 1288 mg L−1, and propionic acid, 1119 mg L−1) and 2270.2 mg L−1 of VFA (predominantly butyric acid, 1339 mg L−1), were obtained, respectively. The thermophilic conditions were scaled up in a two-phase leachate bed reactor to obtain a final stream with a VFA concentration of 7879 mg L−1 composed mainly of butyric acid. Then, the technical feasibility of using the obtained streams as substrates for the production of poly(3-hydroxybutyrate-co-valerate) (PHBV) by Haloferax mediterranei was demonstrated. The PHBV production was found to be related to the butyric acid content, as the PHBV production was 1.4 vs. 0.3 g L−1 when using the streams rich in butyric acid vs. propionic acid, but the monomeric composition was dependent on the presence of propionic acid. A maximum PHVB production of 2.43 g L−1 and PHA accumulation of 44.3% were reached after 120 h of cultivation in bioreactor conditions. The characteristics of the produced PHBV bioplastic were compared with those of a commercial-grade PHA and found to be similar.

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