Cordeiro Cândida Nathaly, Rojas Patricia, Kato Mario T, Florencio Lourdinha, Sanz José Luis
Department of Molecular Biology, Autonomous University of Madrid, 28049, Madrid, Spain.
Department of Civil and Environmental Engineering, Laboratory of Environmental Sanitation, Federal University of Pernambuco, Recife, PE, 50740-530, Brazil.
Appl Microbiol Biotechnol. 2025 Feb 1;109(1):34. doi: 10.1007/s00253-025-13413-5.
The evolution of the bacterial community in an up-flow anaerobic reactor with silicone support, continuously fed with pure glycerol (day 0-293) and crude glycerol (day 294-362), was studied. Biomass from a former glycerol-degrading reactor was used as inoculum. The maximum yield and productivity of 1,3-propanediol (PDO) (0.62 mol.mol-gly and 14.7 g.L.d, respectively) were obtained with crude glycerol. The inoculum had low diversity, with dominance of Lactobacillus (70.6%) and Klebsiella/Raoultella (23.3%). After 293 days of feeding with pure glycerol, the abundance of both taxa decreased to less than 10%, either in the attached biofilm or in the biomass growing in suspension. The genus Clostridium and members of the Ruminococcaceae family then became the majority. In the period after feeding with crude glycerol, Clostridium remained as the majority genus in the biofilm; however, it was partially replaced in the suspension by Eubacterium, a non-glycerol degrading bacterium. This fact, together with the prevalence of other glycerol-degrading genera in the biofilm, such as Caproiciproducens and Lactobacillus, indicated that the bacteria attached to the silicone support were responsible for converting glycerol into 1,3-PDO. Therefore, to increase the 1,3-PDO productivity, a good approach would be to maximize the amount of reactor support. Other genera that do not degrade glycerol, such as Anaerobacter and Acetomaculum, thrived at the expense of cellular decay material. The Canonical Correspondence Analysis demonstrated that the origin of glycerol is an important variable to consider during the bioreactor operation for producing 1,3-PDO, while the glycerol loading rate is not. KEY POINTS: • Microbial community showed robustness in a range of operational conditions. • A significantly high 1,3-propanediol yield can be achieved using crude glycerol. • The attached biofilm appears to be key to the high production of 1,3-propanediol.
研究了在填充硅胶载体的上流式厌氧反应器中细菌群落的演变,该反应器连续进料纯甘油(第0 - 293天)和粗甘油(第294 - 362天)。来自先前甘油降解反应器的生物质用作接种物。使用粗甘油时,1,3 - 丙二醇(PDO)的最大产量和生产率分别为0.62 mol·mol - 甘油和14.7 g·L·d。接种物的多样性较低,以乳酸杆菌为主(70.6%),克雷伯菌属/拉乌尔菌属占23.3%。在用纯甘油进料293天后,无论是附着的生物膜还是悬浮生长的生物质中,这两个类群的丰度均降至10%以下。梭菌属和瘤胃球菌科成员随后成为优势菌群。在用粗甘油进料后的时期,梭菌属在生物膜中仍然是优势菌属;然而,在悬浮液中它被非甘油降解细菌真杆菌部分取代。这一事实,连同生物膜中其他甘油降解菌属(如己糖丙酸杆菌属和乳酸杆菌属)的流行,表明附着在硅胶载体上的细菌负责将甘油转化为1,3 - PDO。因此,为了提高1,3 - PDO的生产率,一个好的方法是最大化反应器载体的量。其他不降解甘油的菌属,如厌氧杆菌属和醋微菌属,以细胞衰亡物质为代价而大量繁殖。典范对应分析表明,甘油来源是生物反应器生产1,3 - PDO操作过程中要考虑的一个重要变量,而甘油负荷率则不是。要点:• 微生物群落在一系列操作条件下表现出稳健性。• 使用粗甘油可实现显著高的1,3 - 丙二醇产量。• 附着的生物膜似乎是1,3 - 丙二醇高产的关键。