Carbon dioxide uptake efficiency by outdoor microalgal cultures in tubular airlift photobioreactors

✍ Scribed by T. Mazzuca Sobczuk; F. García Camacho; F. Camacho Rubio; F. G. Acién Fernández; E. Molina Grima

• Publisher: John Wiley and Sons
• Year: 2000
• Tongue: English
• Weight: 276 KB
• Volume: 67
• Category: Article
• ISSN: 0006-3592
• DOI: 10.1002/(sici)1097-0290(20000220)67:4<465::aid-bit10>3.0.co;2-9

✦ Synopsis

The influence of solar irradiance and carbon dioxide molar fraction of injected CO 2 -air mixtures on the behavior of outdoor continuous cultures of the microalga Phaeodactylum tricornutum in tubular airlift photobioreactors was analyzed. Instantaneous solar irradiance, pH, dissolved oxygen, temperature, biomass concentration, and the mass flow rates of both the inlet and outlet oxygen and carbon with both the liquid and gas phases were measured. In addition, elemental analysis of the biomass and the cell-free culture medium was performed. The oxygen production rate and carbon dioxide consumption rate increased hyperbolically with the incident solar irradiance on the reactor surface. Carbon losses showed a negative correlation with the daily variation of the carbon dioxide consumption rate. The maximum CO 2 uptake efficiency was 63% of the CO 2 supplied when the CO 2 concentration in the gas supplied was 60% v/v. Carbon losses were >100% during the night, due to CO 2 production by respiration, and hyperbolically decreased to values of 10% to 20% in the midday hours. An increase in the carbon fixed in the biomass with the solar cycle was observed. A slight daily decrease of carbon content of the cell-free culture medium indicated the existence of carbon accumulation in the culture. A decrease in CO 2 molar fraction in the injected gas had a double benefit: first, the biomass productivity of the system was enhanced from 2.05 to 2.47 g L -1 day -1 by reduction of CO 2 inhibition and/or pH gradients; and second, the carbon losses during the daylight period were reduced by 60%. The fluid dynamics in the reactor also influenced the carbon losses: the higher the liquid flow rate the higher the carbon losses. By using a previous mass transfer model the experimental results were simulated and the usefulness of this method in the evaluation and scale-up of tubular photobioreactors was established.