Despite their use in commercial applications since the mid-1990s, BFT systems are still
facing serious drawbacks and operational difficulties. For example, the dependency of out-
door systems on prevailing weather conditions often results in fluctuations in water quality
due to changes in microalgae bloom. Therefore, for sustainable aquaculture production,
certain factors such as site location, light intensity, and season of the year should be taken
into consideration when setting up outdoor BFT systems. Furthermore, the concentration of
total suspended solids (TSS) should be carefully monitored. The desirable concentration of
].
therefore necessitate the changing of aerators to increase levels of dissolved oxygen
Sustainability
2021, 13, 7255
10 of 15
•
TAN. Total ammonia nitrogen below 0.5 mg L
−1
indicates that the system is working
properly. An increase in TAN above this level warrants the addition of carbon into
the system.
•
DO. Dissolved oxygen should not fall below 5 mg L
−1
. Below this level, more aerators
should be added to the system to provide more oxygen.
•
Floc volume (FV) should be in the range of 5 to 50 mL L
−1
and this can be monitored
using Imhoff cones. When FV concentrations are above 50 mL L
−1
, sludge should be
removed, and if below 5 mL L
−1
, carbohydrates should be added.
The slow establishment of nitrifying bacteria within the BFT system is also one of
the drawbacks of this technology. It takes more than one month for the initial bioflocs to
develop, which might affect aquatic life at sensitive stages of their life cycle. Luo et al. [
102
]
have recently shown that a strategy of a one-time carbohydrate addition at a C/N ratio
maintained at 20:1 has a good nitrification performance. However, the authors did not
show how fast the nitrifying bacteria were established; thus, more research is needed. De
Morais et al. [
103
] have also shown that increasing the aeration at a rate of 33.75 L/min
in Litopenaeus vannamei (Boone, 1931) biofloc culture speeded up the establishment of
nitrifying bacteria, whereas a low aeration rate slowed down the process. Jiménez-Ordaz
et al. [
104
] have recently demonstrated that the addition of Schizochytrium sp., L. fermentum
(TD19), and two diatoms (Grammatophora sp. and Navicula sp.) can induce the formation
of bioflocs in a hyper-intensive culture of P. vannamei reared in a BFT system. Therefore,
more research is needed to optimize the conditions necessary for the fast establishment of
slow-growing nitrifying bacteria in BFT systems.
Another serious limitation of BFT is high energy costs. Aerators and pumps require
energy for their normal operation and any incident of power failure can cause huge
economic losses. Likewise, high energy costs (hydroelectricity) make BFT systems less
feasible to small-scale farmers and those from developing countries. Hence, there is an
urgent need to search for cheaper and environmentally cleaner sources of energy that
would sustainably permit intensive cultivation and result in maximum profits. Another
important concern of the BFT system is the development of off-flavors (geosmin and 2-
methylisoborneol) that lower the quality and market cost of BFT-produced fish and shrimps.
These off-flavors develop as a result of high turbidity, filamentous cyanobacteria, and
Actinomycetes. Transferring fish and shrimps to clean running water before harvest would
alleviate this problem but this is costly and unsustainable. However, Schrader et al. [
105
]
suggested that lowering the feeding application rates could decrease the production of
off-flavors, particularly 2-methylisoborneol (MIB) in channel catfish (Ictalurus punctatus).
Another strategy is to introduce certain microorganisms, such as those from the Bacillaceae
family, into the BFT system designs as bioreactors. These have been reported to play a vital
role in the degradation of geosmin and MIB [
106
,
107
].
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