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首页> 外文期刊>Journal of Applied Phycology >Optimization of eicosapentaenoic acid production by Phaeodactylumtricornutum in the flat panel airlift (FPA) reactor
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Optimization of eicosapentaenoic acid production by Phaeodactylumtricornutum in the flat panel airlift (FPA) reactor

机译:平板空运(FPA)反应器中Phaeodyylumtricornutum生产二十碳五烯酸的优化

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Biomass and eicosapentaenoic acid (EPA) productivities were investigated in a flat panel airlift loop reactor ideally mixed by static mixers. Growth with ammonium, urea and nitrate as nitrogen source were performed at different aeration rates. Cultures grew on ammonium but the decay of pH strongly inhibited biomass increase. On urea biomass productivity reached 2.35 g L super(-1) d super(-1) at an aeration rate of 0.66 vvm (24 h light per day, 1000 mu mol photon m super(-2) s super(-1)). Aeration rates between 0.33 vvm and 0.66 vvm and maximal productivities on urea were linearly dependent. Productivity on nitrate never exceeded 1.37 g L super(-1) d super(-1). In the range of maximum productivity photosynthesis efficiency of 10.6% was reached at low irradiance (250 mu mol photon m super(-2) s super(-1)). Photosynthesis efficiency decreased to 4.8% at 1000 mu mol photon m super(-2) s super(-1). At these high irradiances the flat panel airlift reactor showed a 35% higher volume productivity than the bubble column. At continuous culture conditions the influence of CO sub(2) concentration in the supply air was tested. Highest productivities were reached at 1.25% (v/v) CO sub(2) where the continuous culture yielded 1.04 g L super(-1) d super(-1) (16 h light per day, 1000 mu mol photon m super(-2) s super(-1)). The average EPA content amounted to 5.0% of cell dry weight, that resulted in EPA productivities of 52 mg L super(-1) d super(-1) (continuous culture, 16 h light per day) or 118 mg L super(-1) d super(-1) (batch culture, 24 h light per day).
机译:在理想通过静态混合器混合的平板气举回路反应器中研究了生物质和二十碳五烯酸(EPA)的生产率。以铵,尿素和硝酸盐为氮源以不同的曝气速率进行生长。培养物在铵上生长,但是pH的下降强烈抑制了生物量的增加。尿素生物量的生产率达到0.63 vvm(每天24小时光照,1000μmol光子m super(-2)s super(-1)的曝气速率达到2.35 g L super(-1)d super(-1) 。 0.33 vvm和0.66 vvm之间的曝气速率以及尿素的最大生产率线性相关。硝酸盐的生产率从未超过1.37 g L super(-1)d super(-1)。在最大生产率范围内,低辐照度(250μmol光子m super(-2)s super(-1))的光合作用效率达到10.6%。在1000μmol光子m super(-2)s super(-1)下,光合作用效率降至4.8%。在这些高辐照度下,平板气举反应器的体积生产率比鼓泡塔高35%。在连续培养条件下,测试了送风中CO sub(2)浓度的影响。最高生产率达到1.25%(v / v)CO sub(2),连续培养产生1.04 g L super(-1)d super(-1)(每天16 h光照,1000μmol光子m super( -2)的super(-1))。 EPA的平均含量为细胞干重的5.0%,因此EPA的生产率为52 mg L super(-1)d super(-1)(连续培养,每天16 h光照)或118 mg L super(- 1)d super(-1)(分批培养,每天24小时光照)。

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