Technical University of Denmark (DTU), Dept. of Chemical and Biochemical Engineering, Center for Bioprocess Engineering, Søltofts Plads, Building 229, 2800, Kgs. Lyngby, Denmark.
Technical University of Denmark (DTU), Dept. of Chemical and Biochemical Engineering, Danish Polymer Center, Søltofts Plads, Building 229, 2800, Kgs. Lyngby, Denmark.
Water Res. 2018 Jan 1;128:255-266. doi: 10.1016/j.watres.2017.10.046. Epub 2017 Oct 23.
Crude glycerol, a by-product from the biodiesel industry, can be converted by mixed microbial consortia into 1,3-propanediol (1,3-PDO) and volatile fatty acids. In this study, further conversion of these main products into polyhydroxyalkanoates (PHA) was investigated with the focus on 1,3-PDO. Two different approaches for the enrichment of PHA accumulating microbial consortia using an aerobic dynamic feeding strategy were applied. With the first approach, where nitrogen was present during the whole cycle, no net production of PHA from 1,3-PDO was observed in the fermented effluent, not even in a nitrogen-limited PHA accumulation assay. Nevertheless, experiments in synthetic substrates revealed that the conversion of 1,3-PDO to PHA was possible under nitrogen limiting conditions. Thus, a different enrichment strategy was formulated where nitrogen was limited during the feast phase to stimulate the storage response. Nitrogen was still supplied during the famine phase. With the latter strategy, a net production of PHA from 1,3-PDO was observed at a yield of 0.24 C PHA/C 1,3-PDO. The overall yield from the fermented effluent was 0.42 C PHA/C substrate. Overall, the PHA yield from 1,3-PDO seemed to be limited, similarly to when using glycerol as a substrate, by a decarboxylation step and accumulation of other storage polymers such as glycogen, and possibly, lipid inclusions.
粗甘油是生物柴油工业的一种副产物,可以被混合微生物群落转化为 1,3-丙二醇(1,3-PDO)和挥发性脂肪酸。在这项研究中,进一步将这些主要产物转化为聚羟基脂肪酸酯(PHA),重点是 1,3-PDO。使用需氧动态进料策略,通过两种不同的方法富集能够积累 PHA 的微生物群落。在第一种方法中,整个周期都存在氮,在发酵废水中没有观察到从 1,3-PDO 净生产 PHA,即使在氮限制的 PHA 积累测定中也是如此。然而,在合成底物的实验中发现,在氮限制条件下,1,3-PDO 可以转化为 PHA。因此,制定了一种不同的富集策略,在饱食阶段限制氮以刺激储存反应。在饥饿阶段仍提供氮。采用后一种策略,从 1,3-PDO 中观察到 PHA 的净生产,产率为 0.24 C PHA/C 1,3-PDO。从发酵废水中的总产率为 0.42 C PHA/C 基质。总的来说,从 1,3-PDO 生产 PHA 的产量似乎受到限制,类似于使用甘油作为底物时,受到脱羧步骤和其他储存聚合物(如糖原和可能的脂滴)的积累的限制。