Acién Fernández F G, Fernández Sevilla J M, Egorova-Zachernyuk T A, Molina Grima E
Department of Chemical Engineering, University of Almería, E-04071 Almería, Spain.
Biomol Eng. 2005 Dec;22(5-6):193-200. doi: 10.1016/j.bioeng.2005.09.002. Epub 2005 Oct 28.
The present study outlines a process for the cost-effective production of 13C/15N-labelled biomass of microalgae on a commercial scale. The core of the process is a bubble column photobioreactor with exhaust gas recirculation by means of a low-pressure compressor. To avoid accumulation of dissolved oxygen in the culture, the exhaust gas is bubbled through a sodium sulphite solution prior to its return to the reactor. The engineered system can be used for the production of 13C, 15N, and 13C-15N stable isotope-labelled biomass as required. To produce 13C-labelled biomass, 13CO2 is injected on demand for pH control and carbon supply, whereas for 15N-labelled biomass Na15NO3 is supplied as nitrogen source at the stochiometric concentration. The reactor is operated in semicontinuous mode at different biomass concentrations, yielding a maximum mean biomass productivity of 0.3 gL(-1) day(-1). In order to maximize the uptake efficiency of the labelled substrates, the inorganic carbon is recovered from the supernatant by acidification/desorption processes, while the nitrate is delivered at stochiometric concentration and the harvesting of biomass is performed when the 15NO3- is depleted. In these conditions, elemental analysis of both biomass and supernatant shows that 89.2% of the injected carbon is assimilated into the biomass and 6.9% remains in the supernatant. Based on elemental analysis, 97.8% of the supplied nitrogen is assimilated into the biomass and 1.3% remains in the supernatant. Stable isotope-labelling enrichment has been analysed by GC-MS results showing that the biomass is highly labelled. All the fatty acids are labelled; more than 96% of the carbon present in these fatty acids is 13C. The engineered system was stably operated for 3 months, producing over 160 g of 13C and/or 15N-labelled biomass. The engineered bioreactor can be applied for the labelling of various microalgae.
本研究概述了一种在商业规模上经济高效地生产13C/15N标记微藻生物质的方法。该方法的核心是一个带有废气再循环装置的鼓泡塔光生物反应器,废气通过低压压缩机进行再循环。为避免培养物中溶解氧的积累,废气在返回反应器之前先通过亚硫酸钠溶液鼓泡。该工程系统可根据需要用于生产13C、15N和13C-15N稳定同位素标记的生物质。为生产13C标记的生物质,按需注入13CO2以控制pH值和提供碳源,而对于15N标记的生物质,则以化学计量浓度供应Na15NO3作为氮源。反应器以半连续模式在不同的生物质浓度下运行,最大平均生物质生产率为0.3 gL(-1)天(-1)。为了最大限度地提高标记底物的吸收效率,通过酸化/解吸过程从上清液中回收无机碳,同时以化学计量浓度供应硝酸盐,并在15NO3-耗尽时进行生物质收获。在这些条件下,对生物质和上清液的元素分析表明,注入的碳中有89.2%被同化为生物质,6.9%留在上清液中。基于元素分析,供应的氮中有97.8%被同化为生物质,1.3%留在上清液中。通过气相色谱-质谱(GC-MS)结果分析稳定同位素标记富集情况,结果表明生物质具有高度标记。所有脂肪酸均被标记;这些脂肪酸中存在的碳超过96%是13C。该工程系统稳定运行了3个月,生产了超过160 g的13C和/或15N标记的生物质。该工程生物反应器可应用于各种微藻的标记。