Outdoor continuous culture of Porphyridium cruentum in a tubular photobioreactor: quantitative analy

The present work reports on the daily cyclic variation of oxygen generation rates, carbon consumption rates, photosynthetic activities, growth rates and biochemical composition of the biomass in a pilot plant continuous outdoor culture of the microalgae Porphyridium cruentum. A linear relationship between the external irradiance and the average irradiance inside the culture was found. In addition, the oxygen generation and carbon consumption rates were found to be a function of the average irradiance inside the culture. A reduction in photosynthetic activity of the cells at noon and recovery in the afternoon was also observed. Therefore, the cells showed a short-term response of parameters such as oxygen generation rate as well as carbon consumption rate with external and average irradiance; a model of photosynthesis rate considering photoinhibition is proposed. This model is a useful tool for the operation and scaleup of tubular photobioreactors, and can be used for determining CO2 requirements of the system. The higher the photosynthesis rates, the lower the carbon losses, ranging from 25% at noon to 100% during the night. The growth rate showed a linear relationship with the daily mean average irradiance inside the culture with a long-term response. Likewise, a linear relationship among the oxygen generation rate and the growth rate was obtained. With respect to the biochemical composition of the biomass, the cells showed a long-term response of metabolic routes to mean daily culture conditions. During the illuminated period, energy was stored as carbohydrates and synthesis of proteins was low. During the night, the stored carbohydrates were consumed. The fatty acid dry weight (DW) content decreased during the daylight period, whereas the fatty acid profile, as total fatty acids, was a function of growth rate. A short-term variation of exopolysaccharides synthesis with solar irradiance was also observed, i.e. the higher the external irradiance the higher the excretion of exopolysaccharides as a protection against adverse culture conditions.

[1]  G. Lepage,et al.  Improved recovery of fatty acid through direct transesterification without prior extraction or purification. , 1984, Journal of lipid research.

[2]  M. Kates,et al.  Lipid components of diatoms. , 1966, Biochimica et biophysica acta.

[3]  J. G. Sanchez,et al.  Cuantificación de ácidos grasos a partir de biomasa microalgal , 1993 .

[4]  J. Pérez,et al.  Nota. Composición nutritiva de la biomasa de la microalga Porphyridium cruentum / Note. Nutrient composition of the biomass of the microalga Porphyridium cruentum , 2000 .

[5]  O. Aozasa,et al.  Sustained production of arachidonic and eicosapentaenoic acids by the red alga Porphyridium purpureum cultured in a light/dark cycle , 1992 .

[6]  R. Appleby,et al.  The distribution and biosynthesis of arachidonic acid in algae , 1969 .

[7]  C. Low,et al.  Productivity of outdoor algal cultures in enclosed tubular photobioreactor. , 1992, Biotechnology and bioengineering.

[8]  A. Vonshak,et al.  Photoadaptation, photoinhibition and productivity in the blue‐green alga, Spirulina platensis grown outdoors , 1992 .

[9]  Michael A. Borowitzka,et al.  Closed algal photobioreactors: Design considerations for large-scale systems , 1996 .

[10]  E. Grima,et al.  Prediction of dissolved oxygen and carbon dioxide concentration profiles in tubular photobioreactors for microalgal culture , 1999, Biotechnology and bioengineering.

[11]  F. G. Fernández,et al.  A model for light distribution and average solar irradiance inside outdoor tubular photobioreactors for the microalgal mass culture. , 1997, Biotechnology and bioengineering.

[12]  F. G. Fernández,et al.  Outdoor culture of Isochrysis galbana ALII-4 in a closed tubular photobioreactor , 1994 .

[13]  A. Richmond,et al.  The feasibility of mass cultivation of Porphyridium , 1985 .

[14]  S. Katoh,et al.  Arachidonic acid production by the red alga Porphyridium cruentum , 1983, Biotechnology and bioengineering.

[15]  E. Percival,et al.  The extracellular polysaccharides of porphyridium cruentum and porphyridium aerugineum , 1979 .

[16]  J. Whyte Biochemical composition and energy content of six species of phytoplankton used in mariculture of bivalves , 1987 .

[17]  Janet R. Stein-Taylor Culture methods and growth measurements , 1973 .

[18]  J. Myers On the Algae: Thoughts about Physiology and Measurements of Efficiency , 1980 .

[19]  R. L. Romero,et al.  Radiation field modelling in photoreactors—I. homogeneous media , 1986 .

[20]  P. Falkowski Primary productivity in the sea , 1980 .

[21]  John S. Burlew,et al.  Algal culture from laboratory to pilot plant. , 1953 .

[22]  W. Beckman,et al.  Solar Engineering of Thermal Processes , 1985 .

[23]  J. Sevilla,et al.  A study on simultaneous photolimitation and photoinhibition in dense microalgal cultures taking into account incident and averaged irradiances , 1996 .

[24]  J. Sevilla,et al.  Modeling of biomass productivity in tubular photobioreactors for microalgal cultures: effects of dilution rate, tube diameter, and solar irradiance , 1998, Biotechnology and bioengineering.

[25]  Yuan-Kun Lee Enclosed bioreactors for the mass cultivation of photosynthetic microorganisms: the future trend , 1986 .

[26]  G. Torzillo,et al.  A two‐plane tubular photobioreactor for outdoor culture of Spirulina , 1993, Biotechnology and bioengineering.

[27]  Giuseppe Torzillo,et al.  Temperature as an important factor affecting productivity and night biomass loss in Spirulina platensis grown outdoors in tubular photobioreactors , 1991 .

[28]  E. Evers,et al.  A model for light‐limited continuous cultures: Growth, shading, and maintenance , 1991, Biotechnology and bioengineering.

[29]  E. Molina Grima,et al.  Outdoor chemostat culture of Phaeodactylum tricornutum UTEX 640 in a tubular photobioreactor for the production of eicosapentaenoic acid , 1994, Biotechnology and Applied Biochemistry.

[30]  H. Guterman,et al.  A macromodel for outdoor algal mass production , 1990, Biotechnology and bioengineering.

[31]  Masahito Taya,et al.  Carbon dioxide fixation in batch culture of Chlorella sp. using a photobioreactor with a sunlight-cellection device , 1996 .

[32]  J. Ramus THE PRODUCTION OF EXTRACELLULAR POLYSACCHARIDE BY THE UNICELLULAR RED ALGA PORPHYRIDIUM AERUGINEUM 1, 2 , 1972 .

[33]  P. Falkowski,et al.  Potential enhancement of photosynthetic energy conversion in algal mass culture , 1987, Biotechnology and bioengineering.

[34]  E. Molina Grima,et al.  A mathematical model of microalgal growth in light-limited chemostat culture , 1994 .

[35]  Michael A. Borowitzka,et al.  Micro-algal biotechnology. , 1988 .

[36]  C. Gudin,et al.  Bioconversion of solar energy into organic chemicals by microalgae , 1986 .

[37]  Y. Collos,et al.  Nitrogen Uptake and Assimilation by Marine Phytoplankton , 1980 .