of Spirulina maxima (equivalent to 0.111 kg m
2
).
Weather conditions in Central Mexico, with high
and practically constant temperature and solar radi-
ation through the year, and the high alkalinity of the
water favor effortless predomination of S. maxima on
Lake Texcoco. The water of the lake flows by gravity
into a sloped spiral raceway, maintaining gentle
agitation. This factory stopped its production in the
mid-1990s due to a long strike that led to the bank-
ruptcy of the company.
0021 The most advanced system developed so far is the
high-rate algal ponds (HRAP) which combines the
treatment of sewage with the simultaneous massive
production of algae. The project was developed by
the Technion Research Center at Haifa, Israel. Basic
infrastructures are shallow canals that add up to a
maximum of 1000 m
2
, equipped with systems for
gentle agitation and aeration. The process is operated
continuously with retention times varying between
2 and 6 days, depending on the season. A steady multi-
culture is established in the system within a few days
of operation. This includes bacteria that degrade or-
ganic compounds, and well-defined algal species,
with Euglena, Chlorella, and Scenedesmus predomin-
ating. The maximum daily productivity reported at
times of maximum solar radiation is 30 g m
2
, with
an average annual production of 7 kg of algae per m
2
.
To recover the cells, aluminum sulfate is added as a
flocculant; the float is then dewatered by centrifuga-
tion and dried in a drum drier to reach a final mois-
ture content of 10%. The final product has been
shown to have an excellent nutritional quality, con-
taining 57.4 g of crude protein per 100 g, and an
amino acid profile superior to the average for soybean
protein. It has been used to complement at least 25%
of fish diet and 10% of poultry diet with no toxic
effects. The resulting effluent can be used directly for
crop irrigation.
0022 Chlorella ellipsoidea is produced in Taiwan for
food use in open ponds with agitation or circulation.
The product is recovered by filtration. In China, pilot-
scale open systems have been used for the production
of Spirulina, mainly S. platensis. Ponds about 100 m
2
,
covered with polyvinylchloride sheets, lead to a daily
production of 10 g m
2
(equivalent to more than 3 kg
per year per m
2
if the production could be maintained
constant through the year). Other microalgae pro-
duced in China in open-air systems are Scenedesmus,
Chlorella, and Anabaena.
Photobioreactors
0023 Photobioreactors are closed systems working either
outdoors or indoors, in which a single species is inocu-
lated to keep a clean-culture operation. Closed culti-
vation systems offer better control of contamination
and cell physiology than open systems, leading to
higher growth and quality of the harvested product,
but manufacturing costs increase.
0024Large systems operating outdoors consist of tubes
covering large areas exposed to sunlight and can be
operated either in batch or continuously. Many
designs have been constructed or proposed at pilot
scale. Tubes are made of either glass or plastic, such as
polyethylene. Since the tubes behave as solar collect-
ors, overheating is a problem. Hence, the tubular
solar receptors must have a temperature control
system, which is usually a water pool. Alternatively,
the use of thermotolerant strains has been proposed
to avoid cooling facilities. Generally, tubes are
grouped in several modules to facilitate control, oper-
ation, and to offer flexibility to the system in terms of
culture volume. CO
2
supply systems such as carbon-
ation towers, pumps for circulating the medium, and
tanks to mix nutrients are attached to the solar recep-
tors. These photobioreactors have been used for the
production of Chlorella, Spirulina, and Scenedesmus.
0025Other designs constructed in Chile up to a scale of
110 m
2
of solar irradiation area consist of a pond
made of cement lined with epoxy resin and covered
with a polyethylene dome. The agitation system is a
paddlewheel. It has been used to produce Spirulina
biomass, reachinga growthdensity of 450–750 mg l
1
.
0026An innovative design, operated in the USA, is based
on the use of oval plastic bags floating on thermal
waters.
0027Photobioreactors operating indoors necessarily
have smaller sizes because artificial light is needed.
Designs can be either plastic tubular systems, or stain-
less-steel fermenter-like reactors with internal illu-
mination to allow maximum light incidence. Their
use is rather limited for SCP production because of
low throughputs; however, they are quite adequate
for the production of algal metabolites with high
added value, such as polysaccharides, carotenes, and
other pigments, polyunsaturated fatty acids, etc.
Harvesting
0028The recovery of microalgal biomass after production
is rather difficult, particularly in large-area lakes, or
when low concentrations occur. Some species, such as
Spirulina platensis, S. maxima,andCoelastrum pro-
biscideum, are easily skimmed off or harvested by
filtration through cloths or screens. Filter presses
can be used as well. Owing to their small cell size
(10 mm), other species need to be harvested by centri-
fugation or flocculation, adding flocculants such as
lime, alum, or polyelectrolytes.
0029After harvesting, the algal biomass must be
dewatered by centrifugation and/or dried. Oper-
ations to dehydrate biomass are normally done by
5272 SINGLE-CELL PROTEIN/Algae