首页> 外文期刊>Journal of Applied Phycology >Utilization of flue gas for cultivation of microalgae (Chlorella sp.) in an outdoor open thin-layer photobioreactor.
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Utilization of flue gas for cultivation of microalgae (Chlorella sp.) in an outdoor open thin-layer photobioreactor.

机译:利用烟气在室外开放式薄层光生物反应器中培养微藻(小球藻)。

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Flue gas generated by combustion of natural gas in a boiler was used for outdoor cultivation of Chlorella sp. in a 55 m2 culture area photobioreactor. A 6 mm thick layer of algal suspension continuously running down the inclined lanes of the bioreactor at 50 cm s-1 was exposed to sunlight. Flue gas containing 6-8% by volume of CO2 substituted for more costly pure CO2 as a source of carbon for autotrophic growth of algae. The degree of CO2 mitigation (flue gas decarbonization) in the algal suspension was 10-50% and decreased with increasing flue gas injection rate into the culture. A dissolved CO2 partial pressure (pCO2) higher than 0.1 kPa was maintained in the suspension at the end of the 50 m long culture area in order to prevent limitation of algal growth by CO2. NOX and CO gases (up to 45 mg m-3 NOX and 3 mg m-3 CO in flue gas) had no negative influence on the growth of the alga. On summer days the following daily net productivities of algae [g (dry weight) m-2] were attained in comparative parallel cultures: flue gas=19.4-22.8; pure CO2=19.1-22.6. Net utilization ( eta ) of the photosynthetically active radiant (PAR) energy was: flue gas=5.58-6.94%; pure CO2=5.49-6.88%. The mass balance of CO2 obtained for the flue gas stream and for the algal suspension was included in a mathematical model, which permitted the calculation of optimum flue gas injection rate into the photobioreactor, dependent on the time course of irradiance and culture temperature. It was estimated that about 50% of flue gas decarbonization can be attained in the photobioreactor and 4.4 kg of CO2 is needed for production of 1 kg (dry weight) algal biomass. A scheme of a combined process of farm unit size is proposed; this includes anaerobic digestion of organic agricultural wastes, production and combustion of biogas, and utilization of flue gas for production of microalgal biomass, which could be used in animal feeds. A preliminary quantitative assessment of the microalgae production is presented..
机译:锅炉中天然气燃烧产生的烟气被用于小球藻的室外培养。在55平方米的培养区光生物反应器中。连续向下沿生物反应器的倾斜通道以50 cm s-1运转的6 mm厚的藻类悬浮液层暴露在阳光下。含有6-8%(体积)CO2的烟气代替了成本更高的纯CO2作为藻类自养生长的碳源。藻类悬浮液中的CO2缓解程度(烟道气脱碳)为10-50%,并且随着烟道气向培养物中注入速率的增加而降低。在50 m长的培养区域结束时,悬浮液中的溶解CO2分压(pCO2)保持在0.1 kPa以上,以防止藻类受CO2限制。 NOX和CO气体(烟道气中高达45 mg m-3 NOX和3 mg m-3 CO)对藻类的生长没有负面影响。在夏季,在比较平行培养中,藻类的日净生产力[g(干重)m-2]达到以下水平:烟道气= 19.4-22.8;纯CO2 = 19.1-22.6。光合有效辐射(PAR)能量的净利用率(eta)为:烟气= 5.58-6.94%;纯CO2 = 5.49-6.88%。为烟道气流和藻类悬浮液获得的CO2的质量平衡已包含在数学模型中,该模型允许根据辐照时间和培养温度来计算向光生物反应器中的最佳烟道气注入速率。据估计,在光生物反应器中可实现烟气脱碳约50%,而生产1千克(干重)藻类生物质则需要4.4千克二氧化碳。提出了农场单位规模综合处理方案。这包括有机农业废弃物的厌氧消化,沼气的生产和燃烧,以及利用烟道气生产微藻类生物质,这些可用于动物饲料。提出了对微藻生产的初步定量评估。

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