Dept. of Biochemical and Pharmaceutical Technology, Faculty of Pharmaceutical Sciences, University of São Paulo, Av. Prof. Lineu Prestes 580, Bl. 16, São Paulo-SP 05508-900, Brazil.
Biotechnol Prog. 2011 May-Jun;27(3):650-6. doi: 10.1002/btpr.581. Epub 2011 Mar 29.
Carbon dioxide released from alcoholic fermentation accounts for 33% of the whole CO(2) involved in the use of ethanol as fuel derived from glucose. As Arthrospira platensis can uptake this greenhouse gas, this study evaluates the use of the CO(2) released from alcoholic fermentation for the production of Arthrospira platensis. For this purpose, this cyanobacterium was cultivated in continuous process using urea as nitrogen source, either using CO(2) from alcoholic fermentation, without any treatment, or using pure CO(2) from cylinder. The experiments were carried out at 120 μmol photons m(-2) s(-1) in tubular photobioreactor at different dilution rates (0.2 ≤ D ≤ 0.8 d(-1) ). Using CO(2) from alcoholic fermentation, maximum steady-state cell concentration (2661 ± 71 mg L(-1) ) was achieved at D = 0.2 d(-1) , whereas higher dilution rate (0.6 d(-1) ) was needed to maximize cell productivity (839 mg L(-1) d(-1) ). This value was 10% lower than the one obtained with pure CO(2) , and there was no significant difference in the biomass protein content. With D = 0.8 d(-1) , it was possible to obtain 56% ± 1.5% and 50% ± 1.2% of protein in the dry biomass, using pure CO(2) and CO(2) from alcoholic fermentation, respectively. These results demonstrate that the use of such cost free CO(2) from alcoholic fermentation as carbon source, associated with low cost nitrogen source, may be a promising way to reduce costs of continuous cultivation of photosynthetic microorganisms, contributing at the same time to mitigate the greenhouse effect.
酒精发酵释放的二氧化碳占葡萄糖衍生燃料乙醇使用过程中所涉及二氧化碳的 33%。由于节旋藻能吸收这种温室气体,本研究评估了利用酒精发酵释放的二氧化碳来生产节旋藻。为此,本研究采用连续培养的方法,以尿素作为氮源,使用未经处理的酒精发酵产生的二氧化碳或来自钢瓶的纯二氧化碳来培养这种蓝藻。实验在 120 μmol 光子 m(-2) s(-1) 的管式光生物反应器中进行,在不同稀释率(0.2 ≤ D ≤ 0.8 d(-1) )下进行。使用酒精发酵产生的二氧化碳,在 D = 0.2 d(-1) 时可达到最大稳态细胞浓度(2661 ± 71 mg L(-1) ),而需要更高的稀释率(0.6 d(-1) )才能使细胞生产率最大化(839 mg L(-1) d(-1) )。该值比使用纯二氧化碳时低 10%,且生物质蛋白含量无显著差异。在 D = 0.8 d(-1) 时,使用纯二氧化碳和酒精发酵产生的二氧化碳分别可获得 56%±1.5%和 50%±1.2%的干生物质蛋白。这些结果表明,利用这种免费的酒精发酵产生的二氧化碳作为碳源,结合低成本的氮源,可能是降低光合微生物连续培养成本的一种有前途的方法,同时有助于减轻温室效应。