Engineering analyses combined with experimental observations in horizontal
tubular photobioreactors and vertical bubble columns are used to demonstrat
e the potential of pneumatically mixed vertical devices for large-scale out
door culture of photosynthetic microorganisms. Whereas the horizontal tubul
ar systems have been extensively investigated, their scalability is limited
. Horizontal tubular photobioreactors and vertical bubble column type units
differ substantially in many ways, particularly with respect to the surfac
e-to-volume ratio, the amount of gas in dispersion, the gas-liquid mass tra
nsfer characteristics, the nature of the fluid movement and the internal ir
radiance levels. As illustrated for eicosapentaenoic acid production from t
he microalga Phaeodactylum tricornutum, a realistic commercial process cann
ot rely on horizontal tubular photobioreactor technology. In bubble columns
, presence of gas bubbles generally enhances internal irradiance when the S
un is low on the horizon. Near solar noon, the bubbles diminish the interna
l column irradiance relative to the ungassed state. The optimal dimensions
of vertical column photobioreactors are about 0.2 m diameter and 4 m column
height. Parallel east-west oriented rows of such columns located at 36.8 d
egrees N latitude need an optimal inter-row spacing of about 3.5 m. In vert
ical columns the biomass productivity varies substantially during the year:
the peak productivity during summer may be several times greater than in t
he winter. This seasonal variation occurs also in horizontal tubular units,
but is much less pronounced. Under identical conditions, the volumetric bi
omass productivity in a bubble column is similar to 60% of that in a 0.06 m
diameter horizontal tubular loop, but there is substantial scope for raisi
ng this value. (C) 1999 Elsevier Science B.V. All rights reserved.