Lactic Acid Fermentation of Carrageenan Hydrolysates from the Macroalga Kappaphycus alvarezii: Evaluating Different Bioreactor Operation Modes

Adam Tabacof, V. Calado, N. Pereira
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Abstract

Lactic acid is a molecule used abundantly in the food, cosmetic, and pharmaceutical industries. It is also the building block for polylactic acid, a biodegradable polymer which has gained interest over the last decade. Seaweeds are fast growing, environmentally friendly, and economically beneficial. The Rhodophyta, Kappaphycus alvarezii, is a carrageenan-rich alga, which can be successfully fermented into lactic acid using lactic acid bacteria. Lactobacillus pentosus is a versatile and robust bacterium and an efficient producer of lactic acid from many different raw materials. Bioreactor strategies for lactic acid fermentation of K. alvarezii hydrolysate were tested in 2-L stirred-tank bioreactor fermentations, operating at 37 °C, pH 6, and 150 rpm. Productivity and yields were 1.37 g/(L.h) and 1.17 g/g for the pulse fed-batch, and 1.10 g/(L.h) and 1.04 g/g for extended fed-batch systems. A 3.57 g/(L.h) production rate and a 1.37 g/g yield for batch fermentation operating with an inoculum size of 0.6 g/L was recorded. When applying fed-batch strategies, fermentation products reached 91 g/L with pulse feed and 133 g/L with constant continuous feed. For control and comparison, a simple batch of synthetic galactose-rich Man-Sharpe-Rugosa (MRS) media was fermented at the same conditions. A short study of charcoal regenerability is shown. A scheme for a third-generation lactic acid biorefinery is proposed, envisioning a future sustainable large-scale production of this important organic acid.
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大藻卡拉胶水解产物的乳酸发酵:不同生物反应器操作模式的评价
乳酸是一种在食品、化妆品和制药工业中大量使用的分子。它也是聚乳酸的组成部分,聚乳酸是一种可生物降解的聚合物,在过去十年中引起了人们的兴趣。海藻生长迅速,对环境友好,经济效益高。红水藻(Kappaphycus alvarezii)是一种富含卡拉胶的藻类,利用乳酸菌可以成功地发酵成乳酸。戊酸乳杆菌是一种多用途、健壮的细菌,是一种从许多不同原料中高效生产乳酸的细菌。在2升搅拌槽生物反应器中,在37°C, pH 6和150 rpm的条件下,对K. alvarezii水解物乳酸发酵的生物反应器策略进行了测试。脉冲进料间歇系统的生产率和产量分别为1.37 g/(L.h)和1.17 g/g,扩展进料间歇系统的生产率和产量分别为1.10 g/(L.h)和1.04 g/g。在接种量为0.6 g/L的条件下,分批发酵的产率为3.57 g/(L.h),产率为1.37 g/g。采用分批进料策略时,脉冲进料发酵产物达到91 g/L,连续进料发酵产物达到133 g/L。为对照和比较,在相同条件下发酵了一批简单的合成富半乳糖Man-Sharpe-Rugosa (MRS)培养基。对木炭的可再生性进行了简短的研究。提出了第三代乳酸生物精炼厂的方案,设想了这种重要有机酸的未来可持续大规模生产。
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