Johann Heinrich von Thünen-Institut, 38116 Braunschweig, Germany.
N Biotechnol. 2012 Jan 15;29(2):211-7. doi: 10.1016/j.nbt.2011.06.015. Epub 2011 Jun 25.
3-hydroxypropionaldehyde (3HPA) is a promising versatile substance derived from the renewable feedstock glycerol. It is a product of glycerol metabolism in Lactobacillus reuteri. Because of toxic effects, the biotechnological production is poor. In this work the biocatalyst lifetime and product formation could be drastically increased. In the established two-step process already applied, cells are grown in the first step under anaerobic conditions, and in the second step the immobilised or suspended biocatalyst is used for 3HPA-production under strict anaerobic conditions. In the first step it was possible to reach a biomass concentration of 5.5g CDW/L (OD(600)≈23.4). In the second step, normally, 3HPA accumulates to a toxic concentration and the reaction stops in less than 60min because of the interaction of 3HPA with cell components. To prevent this, the toxic product is bound to the newly found scavenger carbohydrazide to form the hydrazone. For the first time it was possible to recycle the immobilised biocatalyst for at least ten cycles (overall life time>33hours) in a repeated batch biotransformation with an overall production of 67g 3HPA. The optimal pH-value was between 6.8 and 7.2 at an optimal temperature of 40-45°C. In a single batch biotransformation with suspended resting cells it was possible to produce 150g/L 3HPA as carbohydrazone at an overall productivity of 10.7gL(-1)hours(-1). In a single fed-batch biotransformation at 45°C 138g/L glycerol was converted into 108g/L 3HPA with an overall productivity of 21.6gL(-1)hours(-1). This is the highest 3HPA concentration and productivities reported so far for the microbial production of 3HPA from glycerol.
3-羟基丙醛(3HPA)是一种有前途的多功能物质,由可再生原料甘油衍生而来。它是雷氏乳杆菌甘油代谢的产物。由于毒性作用,生物工艺生产较差。在这项工作中,生物催化剂的寿命和产物形成可以大大提高。在已经应用的两步法中,细胞在第一步中在厌氧条件下生长,在第二步中,固定化或悬浮的生物催化剂在严格的厌氧条件下用于 3HPA 的生产。在第一步中,能够达到 5.5g CDW/L(OD(600)≈23.4)的生物量浓度。在第二步中,通常,由于 3HPA 与细胞成分的相互作用,3HPA 会积累到毒性浓度,反应在不到 60 分钟内停止。为了防止这种情况,有毒产物与新发现的清除剂碳酰肼结合形成腙。首次有可能在重复分批生物转化中至少循环使用固定化生物催化剂 10 次(总寿命>33 小时),总产率为 67g 3HPA。最佳 pH 值在 6.8 和 7.2 之间,最佳温度在 40-45°C。在悬浮休止细胞的单次分批生物转化中,有可能以 10.7gL(-1)小时(-1)的整体生产率生产 150g/L 3HPA 作为碳酰肼。在 45°C 的单次补料分批生物转化中,138g/L 甘油转化为 108g/L 3HPA,整体生产率为 21.6gL(-1)小时(-1)。这是迄今为止报道的微生物从甘油生产 3HPA 的最高 3HPA 浓度和生产率。