Tài liệu Báo cáo Nghiên cứu khoa học Intensive in-Pond raceway production of marine finfish (card vie 062-04): Ministry of Agriculture & Rural Development
Project Progress Report
Project title:
INTENSIVE IN-POND RACEWAY PRODUCTION
OF MARINE FINFISH (CARD VIE 062/04)
MILESTONE 2& 4 REPORT
Two milestone reports are combined in one
for ease in understanding of raceway technology and application of potential users
Michael Burke (QDPI&F, Australia)
Tung Hoang (Nha Trang University, Vietnam)
12/2006
PART 1
Design and performance of floating raceways used to nurse
fingerlings of marine finfish in Central Vietnam
1
Design and performance of floating raceways used to nurse fingerlings of marine
finfish in Central Vietnam
Tung Hoang1*, Phuong T. Luu1, Khanh K. Huynh2, Quyen Q.T. Banh1, Mao D. Nguyen1, Michael Burke3
1 International Center for Training and Research, Nha Trang University, Vietnam
2 Khanh Hoa Fisheries Promotion Center, Vietnam
3 Department of Primary Industries & Fisheries, Bribie Island Aquaculture Research Centre,
Bribie Island, Queensland, Aust...
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Ministry of Agriculture & Rural Development
Project Progress Report
Project title:
INTENSIVE IN-POND RACEWAY PRODUCTION
OF MARINE FINFISH (CARD VIE 062/04)
MILESTONE 2& 4 REPORT
Two milestone reports are combined in one
for ease in understanding of raceway technology and application of potential users
Michael Burke (QDPI&F, Australia)
Tung Hoang (Nha Trang University, Vietnam)
12/2006
PART 1
Design and performance of floating raceways used to nurse
fingerlings of marine finfish in Central Vietnam
1
Design and performance of floating raceways used to nurse fingerlings of marine
finfish in Central Vietnam
Tung Hoang1*, Phuong T. Luu1, Khanh K. Huynh2, Quyen Q.T. Banh1, Mao D. Nguyen1, Michael Burke3
1 International Center for Training and Research, Nha Trang University, Vietnam
2 Khanh Hoa Fisheries Promotion Center, Vietnam
3 Department of Primary Industries & Fisheries, Bribie Island Aquaculture Research Centre,
Bribie Island, Queensland, Australia
1. INTRODUCTION
The development of mariculture in Vietnam requires large number of marine fish
fingerlings for stocking. In recent years, small seeds of high-value fish such as grouper
(Epinephelus spp.), cobia (Rachycentron canadum), barramundi (Lates calcarifer) and
other species are produced in hatcheries, meeting part of the increasing demand by fish
farmers. Not only quantity, but also body size of fingerlings is limited. Marine finfish are
mostly cultured in cages in Vietnam. Stocking, therefore, requires fingerlings larger than
80÷100 mm in total length. In hatcheries, the production of large fingerling is costly and
apparently constrained by limited nursing tank area. Poor survival and difficult husbandry
are recorded also with nursing in ponds (Le Xan 2005).
Floating raceways have been recently trialled successfully for freshwater fish farming
in USA, Australia and Germany. Despite of their relatively high capital and running costs,
the use of floating raceways has a number of advantages including (i) high stocking density
and less predation; (ii) effective feeding and disease management; (iii) easy to handle and
fewer labor required; (iv) taking advantage of natural food in ponds.
In Vietnam, Nha Trang University (the former University of Fisheries) designed a
floating raceway and trialled this system in 2005 – 2006 through the CARD VIE 062/04
project “Intensive in-pond raceway production of marine finfish” coordinated by the
Ministry of Agriculture and Rural Development of Vietnam. This current report presents
the working principles of floating raceways; guidelines for installation and operation of the
version SMART–1 for nursing marine finfish fingerlings; experimental results on
barramundi (Lates calcarifer) covering both financial assessment and dynamics of
raceways. Some initial results on snapper (Lutjanus argentimacus), red drum and red
tilapia (Oreochromis sp.) are also discussed. Target species for coming trials are cobia and
grouper.
2
2. DESIGN OF FLOATING RACEWAY
2.1 Operational principles
Operational principles of floating raceway (FR) is relatively simple. FR can be made of
different materials and looks like a long, narrow tank that float itself or supported by
floating structure. Water in reservoir pond is continuously pumped into one end and
discharged at the other end of the raceway through a system of airlifts, powered by central
air compressor or blower. This helps reduce power costs and increase dissolved oxygen
concentration. Fish are nursed or grown in raceways at high densities, fed with formulated
feed. In addition, plankton in reservoir pond is an important supplementary feed source for
small fish. To keep fish from escaping, a screen is installed at the outlet of raceways. Net is
also used to cover the raceway’s surface to protect fish from predation. Floating raceways
should be designed to maintain high exchange rate, enable waste collection and create a
quiet area for feeding. In case chemical treatment is needed, raceways become ‘close’
tanks when the airlift operation is ceased and its outlet is blocked.
Depending on biological requirement of the cultured species, floating raceways can be
put in relatively deep pond containing either fresh, brackish or marine water. Reservoirs
have enormous potentiality for the application of this farming system. However, electricity
is required for operation of air compressor or blower.
2.2 Pond
The rectangular reservoir pond is 2000 m2 (Fig. 1). Pond should be built on
impermeable soil or lined with plastic. Pond bank is 1.5 slope and 1.8 – 2.0 m wide,
making it convenient for daily management and harvesting. Pond bottom should be flat and
inclines to outlets. The higher water level in pond, the better it is. Minimum water depth is
1.6 ÷ 1.7 m. Conversely, in case of low water levels, the airlift system will take up wastes
and mud from pond bottom into raceways. The reservoir pond is partitioned by a plastic
wall placed in the middle of the pond, directing water to flow around with the aid of a 2-hp
paddle-wheel.
2.3 Floating raceways
Floating raceways version SMART-01 are small in size, used to nurse marine finfish
from small sizes to fingerlings. These are made of fiberglass – the most appropriate
material in Vietnam which is durable, weather proof and easy to clean or move around.
Despite its higher cost than other simple materials, fiberglass raceways have demonstrated
a worthy investment. SMART-1 has a trapezoid-shape (3.5m3 volume, 3.5×0.8×1.0m), 30o
3
slopped at both heads (Fig. 2). One head of the raceway is connected with an airlift system.
The other is attached with a screen to avoid fish escape and predators. At the inlet side of
the raceway, a panel is put to drive water downwards.
Overpass
Floating raceways
Sluice
Air pipeline Air compressor
Wall
Aerator
1.8 – 2 m
1.8 m
Bank
Wall
b
Figure 1: Pond and in-pond floating raceways
2.4 Airlifts
The airlift s ncludes four PVC ∅90-mm pipes. Each pipe is 100 cm long,
attached togethe
raceway. This fra
side of this fram
Air flow is contr
on the lower side
push water up.
capacity” of the a
2.5 Air comp
Water is pum
upon the numbe
six floating racew
ystem ir by a rectangular frame made
me also has a function of bringin
e is connected with an air compr
olled by a plastic valve. Four sma
of the supporting frame, one for
The distance from water surfac
irlifts is dependent upon the pow
ressor
ped into the raceway by an air c
r of airlifts and desired flow rate
ays with a total of 24 airlifts) use
4of PVC ∅21-mm pipes, fixed into the
g air into the airlifts (Fig. 3). The upper
essor or a blower by a soft plastic pipe.
ll holes (3.0 mm in diameter) are drilled
each airlift, allowing air to flow in and
e to these holes is 80 cm. “Pumping
er of air compressor or blower used.
ompressor whose capacity is dependent
. The SMART-01 system (comprises of
s an ANLET BSR-40 air compressor (3
HP or 2.2 KW; Made in Japan). The amount of compressed air is 66 m3 per hour. While
operating, each airlift can pump about 86÷87 L of water per minute.
3.5 m
3.7 m
0.9m
0.6m 0.25m
2.5m
Outlet
Airlifts
Inner side Outer side
Hole to
set airlift
Groove to
install baffleGroove to install
screen
Outlet a
Figure 2: Structure of SMART-01 b
Air
Incoming water
Coming-out water
Air vent
Figure 3: Structure of airlift system
In order to ensu fficient dissolved oxygen and well prepare technical failure,
two air compressors are used in turn. Each operates for 12 hours per day. The air line that
connects the air compressor and the airlift system is designed to end as a rectangular loop
around the su rting pontoon. This helps equalize the amount and pressure of compressed
air at all positions in the system, allowing all the a operate at the same rate.
5irliftsd forre suppo
2.6 Supporting pontoon
A pontoon is used to support the floating raceways. This system was constructed using
6×12 cm blocks of wood and 200-L HDPE drums. These materials are locally available
and often used to make spiny rock lobster cages. The pontoon is rectangular in shape (510
× 750 cm) and is divided into six chambers. The width of each chamber is 95 cm, enabling
convenience while lifting or lowering the floating raceways. Side walkway was made
around the pontoon for daily management and husbandry practices (Fig. 4). The SMART-
01 system uses 17 HDPE drums arranged equally to support the pontoon, sufficiently
enabling the attached raceways always float on the water surface when technicians are
feeding the fish or cleaning the raceways. Six raceways are hung on the raft by Ø14 mm
bolts (450 mm long). This helps keep the raceways emerged 5÷10 from the water surface
Nonetheless, as the raceways are attached to the pontoon, their floatability is dependent
upon the pontoon’s floatability.
a’c c’
6
1
2
1 b b’
3 cross section
topdown a
6 6 5
3 4
outflow side Inflow side
Figure 4: Structure of floating raft supporting raceways
Notes: 1: Floating
raceways
2: Float
3: Airlifts
4: Outlet Screen
5: Bolds hanging raceways
6: Air supply
2.7 Installation and operation
Firstly, the supporting pontoon is assembled and put into the reservoir pond. PVC and
soft plastic pipes were then used to connect the air compressor with the raceways. When
using PVC pipes, it is better to put them underground to prevent damage caused by UV ray
and heat of sunshine. As the air coming off the compressor is very hot, the first segment of
the pipe that attaches to the compressor must be heat-resistant or made of zinc, and is about
6
six meters long. Next, the raceways, airlifts and regulating valves are installed. The
compressor ANLET BSR 40 is capable of operating six raceways and one separate air
outlet for emergency use or when additional aeration in raceways is needed, e.g. during
therapeutic treatment or harvesting.
The top baffle, once installed will direct incoming flows downwards and velocity of
surface current is nearly zero. This helps create a quiet area for feeding behind the baffle.
In addition, the downwards flow will push faeces and uneaten feed toward the end of
raceways. Part of this waste will overflow through the raceway’s outlet. The rest is
accumulated at the end of the raceways and will be daily siphoned out. The newest system
SMART-02 has a waste trap for ease in maintenance.
Key environmental parameters such as salinity, pH, NH4-N, total dissolved solids
(TDS) and temperature are equivalent between the raceways and the reservoir pond.
Therefore, good control of water quality in pond will ensure good nursing environment in
raceways. Thanks to the airlifts, dissolved oxygen levels of water in raceways well meet
fish’s requirement. However, regular attention should be paid to the aeration system
because, by any means, if this system ceases (e.g. due to no power or technical problems),
fish mortality due to lack of oxygen is extremely high. When nursing species that need
natural foods, fertilizers should be used to promote plankton growth in the reservoir pond.
During operation, the aeration system must be regularly checked. As density of
fingerlings in raceways is very high, any problem related to air loss is a danger to fish.
Two air compressors should be used in turn to prolong longevity and minimize damages
because of overwork. In geographical areas where electricity is not reliable, it is advisable
to prepare a petrol-operated generator . Farmers can adjust the amount of air and number of
airlift to control water exchange rate as well as velocity of current in raceways that best
suit the cultured species.
The airlifts will underperform if being bio-fouled. Thus, this system must be cleaned
periodically. Cleaning raceways can be conducted easily by using brushing along the inner
sides and bottom of raceways. However, when nursing species which is sensitive to
turbulence like barramundi, it had better not clean raceways daily.
3. EVALUATING PERFORMANCE OF SMART-01 ON BARRAMUNDI
3.1 Experimental method
Barramundi fingerlings (15÷20 mm total length) were locally produced and
transported to the trial site at Ninh Loc, Khanh Hoa which is belong to the Khanh Hoa
7
Fisheries Extension Center. Stocking density was 10,000 fish per raceway or 3.3 fish/L.
Two trials were conducted; each used three raceways. The raceways were chlorinated at
100 ppm before used. The total length and body weight of fish are determined after two-
day acclimation.
Fish were fed with INVE and Grobest pellet (granular size 800÷1200 µm; crude
protein content 42÷56%). The former feed was used for younger stages in hatchery. In the
first trial, fish were fed with INVE during the first week and then weaned to Grobest. In
the second trial, fish were fed merely with Grobest pellet to reduce feed cost. The amount
of feed is about 2÷18% of body weight depending on development stages and actual
consumption. Fish were fed every hour 06:00 to 18:00. Feeding load was adjusted in the
next feeding based on actual consumption of the current feeding.
Key environmental parameters such as pH, dissolved oxygen (DO) and temperature
were monitored daily at 08:00 and 14:00, both in raceways and in the reservoir pond. Other
factors include total dissolved solids (TDS), total ammonium (NH3-N) and salinity were
measured every five days; total suspended solid every 7 days. Sampling plankton at inlet
and outlet of raceways, and in the reservoir pond was also conducted weekly to observe
changes in species composition and evaluate “filtration efficiency” of the raceways.
Artificial dye and small buoys were used to study the dynamics of water in the raceways.
Every five days, 50 fish from each raceway were randomly collected. Total length
and body weight were measured and recorded. Fish health was also assessed by visual
examination. The survival rate was determined at the end of the experiments. The first trial
lasted for three weeks and the second trial lasted for 5 weeks. The total length of the nursed
fish was 60÷80 mm and 80÷100 mm, respectively at the end of the first and second trials.
Survival, growth and size variation of nursed fish; profit margin and profit per unit of
investment were used for overall assessment.
3.2 Operation of raceways and capacity of water exchange
Flow rate from the reservoir pond to raceways is about 350 L/min. The use of
artificial dye to estimate exchange rate revealed that water in raceways is completely
exchanged every 15 mins (Fig. 1). This ensures relatively similar water quality between the
in the reservoir pond and the raceways, except for DO and TSS (Table 1&2). DO of water
in the raceways is always over 4.0 mg/L and higher than that in the reservoir pond through
effective operation of the airlifts. TSS in raceway is higher than in pond due to
accumulated faeces of fish and uneaten feed.
8
When operating without the top baffle, the average velocity of surface current is 35
cm/s. When the top baffle is used, the water flows downwards and aside with the bottom of
the raceway. This forms a quiet area behind the top baffle for feeding and keep feed pellets
in the raceway. Furthermore, suspended solids are brought out the raceway into pond more
easily. Larger waste is accumulated at the end of raceway, making it easy for daily
cleaning. Examination of the plankton samples showed that the diversity was similar
between the raceways and in the reservoir pond. However, plankton biomass in raceway is
higher than in pond (Table 1), demonstrating its plankton capturing efficiency.
hút 2 - 3 phút
5 - 6 phút 7 - 8 phút
11 - 13 phút 15 - 20 phút
T?
ư?c
Lư?i ch?nscreen? ng nâng nAirlifts
m ch?nplate
0 p0 min
Figure 5: Water exchange rates between raceways and pond (gray area indicates water
mixed with artificial dye)
Table 1 : Water quality in raceway and pond during the first trial. Data in the same rows
with different superscripts are statically different (P < 0.05)
Factors Pond Raceway 3 Raceway 4 Raceway 5
DO (ppm) Morning 3.95 ± 0.16a 4.55 ± 0.14b 4.54 ± 0.14b 4.60 ± 0.13b
Afternoon 5.55 ± 0.17a 5.60 ± 0.16a 5.61 ± 0.17a 5.67 ± 0.16a
Temperature (oC) Morning
Afternoon
pH Morning
Afternoon
Salinity (ppt)
31.6 ± 0.16a 31.6 ± 0.16a 31.6 ± 0.16a 31.6 ± 0.16a
33.4 ± 0.25a 33.3 ± 0.25a 33.3 ± 0.25a 33.3 ± 0.25a
7.6 ± 0.02a 7.6 ± 0.01a 7.6 ± 0.02a 7.6 ± 0.02a
7.6 ± 0.02a 7.6 ± 0.02a 7.6 ± 0.02a 7.6 ± 0.02a
22 ± 0.12a 22 ± 0.12a 22 ± 0.12a 22 ± 0.1a
9
Table 2 : Water quality in raceway and pond during the second trial. Data in the same rows
with different superscripts are statically different (P < 0.05)
Factors Pond Raceway 1 Raceway 2 Raceway 3
DO (ppm) Morning 5.85 ± 0.09a 5.86 ± 0.09a 5.80 ± 0.12a 5,80 ± 0,10a
Afternoon 11.02 ± 0.24a 8.05 ± 0.20b 8.09 ± 0.21b 8,22 ± 0,21b
Temperature (oC) Morning 30.2 ± 0.10a 30.1 ± 0.10a 30.1 ± 0.10a 30.1 ± 0,10a
Afternoon 32.6 ± 0.30a 31.1 ± 0.20b 31.1 ± 0.20b 31.1 ± 0.20b
pH Morning 8.1 ± 0.01a 8.0 ± 0.02a 8.0 ± 0.02a 8.0 ± 0.02a
Afternoon 8.4 ± 0.01a 8.3 ± 0.02b 8.3 ± 0.02b 8.3 ± 0.02b
Salinity (ppt) 29 ± 0.30a 29 ± 0.30a 29 ± 0.30a 29 ± 0.30a
TSS (ppm) 63.8 ± 8.93a 111.1 ±
19.77b
92.5 ± 14.88a 92.4 ± 13.33a
TDS (ppm) 1309 ± 48.9a 1357 ±
57.5a
1334 ± 59.1a 1321 ± 71.0a
NH4+ (ppm) 0.13 ± 0.01a 0.13 ± 0.01a 0.13 ± 0.01a 0.13 ± 0.01a
Outflow
water
top baffle Screen
Airlifts
beh
mor
fish
the
± 0
Coe
tota
with
imp
from
Inflow water
Figure 6: Dynamic of flows in pond
3.3 Growth rate of f
Nursed barramundi in raceways grew fast. They fed
avior while feeding and did not eat in the dark. Feeding
ning and late afternoon. Stomach examination of the nu
larger than 20 mm in total length hardly used zooplankto
first trial, the average body weight and total length (± S.E
.05 cm, respectively after 15 days of nursing. Surv
fficient of variation was 23.8 ± 0.83 % in term of weigh
l length. Estimated food conversion ratio (FCR) is 0.83 ±
nursing barramundi in earthen ponds or concrete tank
rovements.
Another separate experiment showed that growth and s
20 mm to 80 mm are not different when fed with INVE
10ish actively, showed aggressive
was most active in the early
rsed barramundi showed that
n (Luu The Phuong 2006). In
.) was 2.36 ± 0.07 g and 5.13
ival rate was 81.9 ± 1.0%.
t and 11.7 ± 0.28 % in term of
0.01 (Table 3). In comparison
s, these results are significant
urvival of barramundi nursed
or Grobest pellets (Table 4).
Nevertheless, the cost for Grobest pellet is only 1/5 of INVE pellets. The aim to reduce
feed cost, however, was not successful in the second trial where Grobest pellets were
merely used. As the fish got used to INVE feed in the hatcheries, they were not interested
in Grobest pellets. Furthermore, water quality was lower than that for the first trial. Pond
water had been kept for 10 months and salinity was higher (Table 3). Fish were infected
with copepod parasites Caligus. Consequently, hydroperoxide (H2O2) at 150 ppm was
used to treat fish in raceways for 20 – 30 mins. Although relatively effective, it was one of
the reasons for slow growth and lower survival of fish in the second trial. The overall
performance of the second trial was, therefore, inferior than the first one.
As a result, fish growth was not high for the second trial. Specific growth rate of
weight and length of fish are 4.66 ± 0.05 %/day and 1.44 ± 0.03 %/day in the first and the
second trials, respectively. At the end of the trial, the average total length was 10.03 ± 0.23
cm; average body weight was 16.36 ± 1.28 g. Average survival rate of fish was 53.43 ±
1.39%, not as high as in the first one. However, duration of this batch is three times as long
as the first one. Average rate of graded population of body weight is much higher than the
trial I (109.23 ± 3.36 %). Feed conversion rate (FCR) of the trial 2 is 2.8 ± 0.15.
Table 3: Performance of nursed barramundi
Trial I (15 days)
Norms Raceway 3 Raceway 4 Raceway 5 Average
L2 (cm) 5.05 ± 0.09 5.22 ± 0.08 5.12 ± 0.09 5.13 ± 0.05
W2 (g) 2.4 ± 0.12 2.24 ± 0.09 2.5 ± 0.14 2.36 ± 0.07
SRGL (%/day) 3.37 ± 2.21 3.81 ± 2.35 3.59 ± 2.06 3.59 ± 0.13
SRGW (%/day) 9.34 ± 3.08 9.04 ± 3.67 9.40 ± 3.11 9.26 ± 0.11
Survival (%) 80 82.7 83.1 81.93 ± 0.97
CVW (%) 24.80 ± 8.04 22.15 ± 4.46 24.46 ± 9.05 23.8 ± .83
CVL (%) 11.21 ± 1.38 11.71 ± 0.91 12.19 ± 1.34 11.7 ± 0.28
FCR 0.83 0.81 0.85 0.83 ± 0.01
Trial II (45 days)
Norms Raceway 1 Raceway 2 Raceway 3 Average
L2 (cm) 9.65 ± 0.16 10.00 ± 0.16 10.45 ± 0.21 10.03 ± 0.23
SRGL (%/day) 1.40 ± 0.30 1.43 ± 0.29 1.50 ± 0.25 1.44 ± 0.03
W2 (g) 14.38 ± 0.82 15.95 ± 0.84 18.75 ± 1.46 16.36 ± 1.28
SRGW (%/day) 4.56 ± 0.78 4.66 ± 0.72 4.75 ± 0.67 4.66 ± 0.05
Survival (%) 51.1 55.9 53.3 53.43 ± 1.39
CVW (%) 105.27 ± 26.21 106.50 ± 26.27 115.92 ± 33.05 109.23 ± 3.36
CVL (%) 11.02 ± 0.94 10.70 ± 1.10 10.21 ± 1.01 10.64 ± 0.24
FCR 2.5 3 2.9 2.8 ± 0.15
W2, L2: Body weight and total length of fish at the end of the trial
SRGL: Specific growth rate of total length of fish
SRGW: Specific growth rate of body weight of fish
11
CVW (%): Coefficient of variation of weight
CVL (%): Coefficient of variation of total length
Table 4: Performance of barramundi nursed with three different diets: INVE, Grobest and
trash fish after 42-days. Data in the same row with different superscript are statistically
different (P<0.05)
Norms INVE Grobest Trash fish
L2 (mm) 7.69 ± 0.91a 7.44 ± 0.94a 6.92 ± 1.07b
W2 (g) 5.55 ±2.1 5.00 ±1.99 4.33 ± 1.64
SRGL (%/day) 0.013 ± 0.002 0.012 ± 0.001 0.012 ± 0.001
SRGW (%/day) 0.039 ± 0.01 0.038 ± 0,01 0.037 ± 0.001
Survival (%) 98.0 ± 0.63a 82.3 ± 1,63b 74.1 ± 1.63c
Observed dead fish (%) 1.16 ±1.09 6.23 ±2.83 10.72 ±2.83
CVW2 (%) 34.0 ± 7.1 39.0 ± 5.3 38.5 ± 1.9
CVL2 (%) 11.1 ± 1.3 12.8 ± 1.0 15.2 ± 0.7
FCR 0.87 0.90 4.85
3.4 Economic analysis
Operation cost for the first and the second trials was VND 28,802,500 and VND
37,040,000. At harvest, current price was VND 2,500/fish for the first trial and VND 3,000
/fish for the second trial. Thus, calculated profit for the trial was VND 32,947,500 and for
the second trial was VND 10,960,000. Profit rates of the two trials was 1.14 and 0.30,
respectively (Table 5&6).
Table 5: Economic analysis for the first trial (15 days; currency: VND)
Item Unit Quantity Cost price Total
Seed cost fish 30,000 800 24,000,000
Feed cost kg 35 17,000 595,000
Labor cost month 0.5 1,000,000 500,000
Depreciation of fixed assets month 0.5 970,000 485,000
Fuel cost (diesel) L 5 4,500 22,500
Electricity cost (air machines) KW 800 1,500 1,200,000
Other costs 2,000,000
Total costs 28,802,500
Total income fish 24,700 2,500 61,750,000
Profit 32,947,500
Profitable rate (Profit/Total costs) 1.14
12
Table 6: Economic analysis for the second trial (45 days; currency: VND)
Item Unit Quantity Cost price Total
Seed cost Fish 30,000 800 24,000,000
Feed cost Kg 120 17,000 2,040,000
Labor cost month 1.5 1,000,000 1,500,000
Depreciation of fixed assets month 1.5 970,000 1,455,000
Fuel cost (diesel) L 10 4,500 45,000
Electricity cost (air machines,
paddle-wheel) KW 4,000 1,500 6,000,000
Other costs 2,000,000
Total costs 37,040,000
Total income Fish 16,000 3,000 48,000,000
Profit 10,960,000
Profitable rate (Profit/Total costs) 0.30
The profitable rate of the second trial was low because of fish disease and long
duration (i.e. higher electricity cost). Therefore, the nursery environment must be well
control to shorten duration and reduce production costs.
4. LIMITATION OF SMART-01 AND SOLUTION
The two trials have revealed a number of limitations in design of SMART-01. As the
raceways are attached on the pontoon, their mobility is limited and their floatability is
completely dependent upon that of the pontoon. When many people step on the pontoon,
the efficiency of the airlifts are severely affected as the openings where the air is released
are pushed deeper. Further, it is difficult to clean the airlifts. Although accumulated wastes
(at the end of the raceway) can be siphoned easily, SMART-01 does not have a waste
collector. These disadvantages will be improved in SMART-02, an improved version of
SMART-01. This newly-designed raceway is made of fiberglass; 6.0 m3 in volume; self-
float and equipped with a small air compressor. The airlifts of SMART-02 are designed to
float independently off raceways, easy to assemble and clean. Water intake is from the
surface. Therefore, SMART-02 can be put in ponds that are shallower. Fish and waste on
the pond bottom are kept away from the intake water. Both the inlet and outlet of the
raceway are redesigned for better performance and ease in management.
ACKNOWLEDGEMENT
This report uses results of the Project “Intensive in-pond raceway production of marine
finfish’ CARD VIE 062/04 funded by CARD (Collaboration for Agriculture Research &
13
Development) program through Ministry of Agriculture and Rural Development of
Vietnam. The research team would like to thank the sponsor, Nha Trang University,
Institute for Ship Building and Equipment, Khanh Hoa Fisheries Promotion Center, a
number of students of Nha Trang University (Mr. Luu The Phuong, Mr. Nguyen Van
Quyen, Mr. Dam Thanh Ngoc, Ms. Tran Thi Nhat Huong and Mr. Nguyen Phi Thang) and
the following faculty members: Dr . Nguyen Huu Dung, Dr. Nguyen Thi Hoa, Mr. Phan
Van Ut, Mr. Bui Ba Trung, Dr. Hoang Bich Mai and Ms. Mai Thi Bich Hanh for their
valuable help during the implementation of the project.
REFERENCES
Dam T. Ngoc (2006) Effect of some types of feed on growth, survival and size variation of
barramundi (Lates calcarifer Bloch 1790). Thesis. Nha Trang University. (In
Vietnamese).
Lai D. L. Binh (2006) Procedure of nursing barramundi fingerlings from 1 – 45 days after
hatching and determining effect of densities of nursed fingerling on growth, survival
and size variation. Thesis. Nha Trang University. (In Vietnamese).
Le Xan (2005) Results of research on reproduction and culture some species of marine and
brackish fish in Vietnam in recent years, orienting for coming researches. In:
Proceedings of the Conference on research and application science and technology in
aquaculture. Agriculture Publishing House, Ho Chi Minh city, pp. 541-549. (In
Vietnamese).
Luu T. Phuong (2006) Application float raceways to nurse barramundi (Lates calcarifer
Bloch, 1790) from 2 – 8 cm total length. Master thesis. University of Agriculture 1,
Ha Noi. (In Vietnamese).
Nguyen V. Su (2005) Developing tendency of marine fish reproduction technology. Tap
chi Thuy san 3: pp. 28-29. (In Vietnamese).
Tran T. N. Huong (2006) Evaluating the plankton exchange efficiency between reservoir
pond and floating raceways at Ninh Loc, Ninh Hoa, Khanh Hoa. Thesis. Nha Trang
University. (In Vietnamese).
Kunvankij P. (1986) Biology and culture of seabass (Lates calcarifer Bloch, 1790). NACA
Training Manual Series No. 3.
Lee C.S. (2003) Biotechnological advances in finfish hatchery production: a review.
Aquaculture 227: pp. 439 – 458.
14
PART 2
In-Pond Raceway Technology for Marine Finfish Nursery
Production and Grow-Out Developed and Tested
– Australian Component
15
In-Pond Raceway Technology for Marine Finfish Nursery Production and Grow-Out
Developed and Tested – Australian Component
M.J. Burke1, B. Chilton1, L. Dutney1, B. Russell1, A. Collins2 and T. Hoang3
1Department of Primary Industries and Fisheries, Bribie Island Aquaculture Research Centre, Bribie
Island, Queensland, Australia.
2Department of Premier and Cabinet, International Collaborations, Brisbane, Queensland, Australia.
3Nha Trang University, International Centre for Research and Training, NHATRANG City , Vietnam
Correspondence: Michael Burke, Bribie Island Aquaculture Research Centre, PO Box 2066 Bribie Island,
Queensland, 4507 Australia. michael.burke@dpi.qld.gov.au
Introduction
Aquaculture plays an important role in the development of Vietnam’s economy and
has been widely considered as an effective means for poverty alleviation by the FAO. The
country aims to produce 2 million tons of aquaculture products, mainly with marine
species, by 2010. This ambitious target has been supported by a great amount of financial
and technical assistance from the Ministry of Fisheries and several international agencies
including CARD. In Australia, aquaculture has been the fastest growing primary
production sector over the last five years with increasing interest in species like
barramundi, yellowtail kingfish, and more recently grouper and cobia.
Nonetheless, growth of the marine finfish industry in both countries has been
constrained by the absence of cheap, robust production technologies that alleviate the
negative environmental impacts associated with marine aquaculture. In Vietnam, marine
fish are farmed mainly in small sea cages and partly in coastal ponds with wild-caught
fingerlings. In Queensland the traditional sea cage approach to marine fish farming is also
viewed as damaging to coral reefs and other sensitive aquatic habitats. Intense scrutiny of
sea-cage operations indicates these are limited prospects for marine fish farming in
Queensland’s inshore waters. New sustainable yet profitable land based production
methods must be employed in order to return value from the ongoing effort into marine
finfish production. This need is heightened considering that prawn farmers are seeking
alternative cropping opportunities in the wake of global oversupply and the impact of
cheap imports on Australian prawn markets. Currently, no cost effective commercial
systems are available for the intensive production of marine finfish in closed ‘zero
discharge’ systems. Tank based marine recirculation facilities are cost prohibitive and
16
would fail to take advantage of Queensland’s favourable climate and existing pond
aquaculture infrastructure.
This CARD project will address the aforementioned issues by developing a new and
more sustainable farming system for coastal areas with also potential for application to
inland waters. The developing system combines the innovative design of floating raceways
(FRs) with the concept of bioremediation. FRs, either made of plastic or cheap materials,
have been trialled successfully in Japan, Australia and US. They function as flow through
culture units that exchanges water at a rapid constant rate, thus enabling intensive stocking
rates (up to 100 kg/m3) at low capital and operational cost. In comparison to net cages,
FR’s return lower FCR, produce less waste (up to 30%) and require almost half the labour.
Further, a combination of FR’s and bioremediating secondary crops could result in a
closed/semi-closed system that would help remedy environmental impacts of marine
aquaculture. A special feature of this developing system is its high applicability to small-
scale farms using existing infrastructure with no major change in pond design. This project
is expected to help boosting production of marine fish fingerlings and better use the
existing shrimp ponds, of these many are abandoned, in coastal areas. These fit nicely into
the CARD’s framework and aims, i.e. promoting productive technology addressing social,
environmental and human resource development issues.
Figure 1. In-Pond Floating Raceway in Grow-Out Pond/Reservoir at BIARC.
17
This project aims to develop the larval rearing and nursery capacity of marine finfish
growers in Vietnam that is accessible, cost effective and environmentally sustainable.
Through the targeted use of in pond floating raceways (FR) this project will assistance
farmers develop their own intensive but durable and technically manageable larval rearing
capacity. This capacity will be used to improve fingerling supply to the industry which is
currently both costly and limited. In addition, advanced nursery capacity will also be
developed using the same principles. Grow out of finfish in raceways to market size will
also be investigated in this project in conjunction with Australian researchers. Researchers
from the Queensland DPI&F will provide expertise in systems management, water quality
management and waste remediation. Species proposed for study include grouper, cobia and
barramundi. All activities will be conducted using ‘zero discharge’ principles where there
is no net discharge of effluent. Information form these activities will be used to train staff
from the UoF, its students, industry and other relevant stakeholders. Active involvement
and contribution of different stakeholders will make this research highly relevant and
applicable to the local aquaculture industries.
During 2005/06 at the Bribie Island Aquaculture Research Centre (BIARC), grow-out
trials for both mulloway (Argyrosomus japonicus) and the sand whiting (Sillago ciliata)
have run for over 18 months with both species reaching an acceptable market size within
this time. Two different sized raceways were used (Fig.3) – Nursery Raceways (whiting)
with a working volume of 3,600 litres and Grow-Out Raceways (mulloway) with a
working volume of 20,000 litres. Both were assessed for their capacity to produce market
sized fish but with the two different species having large differences in both market size
and growth rate. Whiting in the Australian market can be seen at premium prices from 60
grams onwards. The mulloway trial, of which fish have now reached over 1 kg, will
continue to grow fish for a further 6 months into their premium price/size category of 2 -
2.5 kg.
Materials and Methods
In-Pond Floating Raceways
Floating raceways at BIARC are simply constructed with treated hardwood floating
platforms supported by 200 litre sealed plastic chemical storage drums (Fig.1 & 2). The
raceway itself is constructed of 2mm high density polyethylene (HDPE) secured, and
18
essentially suspended from, the floating platform and end gates affixed to allow water both
in and out through oyster mesh ‘windows’ but having the capability to retaining fish and
even plankton if desired. Mesh size of these ‘windows’ varies according to species and life
stage. The mesh ‘windows’ sit and slide in aluminium window frames (Fig.4) that are
secured with 316 stainless steel screws and C-cup washers to the two end walls. The end
walls are secured to the longitudinal section of the raceway by butting the two HDPE
sheets together perpendicularly and securing (again with 316 stainless steel screws and C-
cup washers) both to a 20 mm x 20 mm strip of compressed recycled plastic cut to the
appropriate length (Fig.4) . More detailed construction information is contained in the
Plan and Isometric drawings below (Fig.7&8).
Figure 2. Raceway floating platform construction
Airlifts and Air Supply
A bank of eighteen PVC Ø90 mm pipes supplies air and water to each of the 20,000 litre
grow-out raceways and is capable of delivering >1500 l/min or a 100% exchange in less
than 15 minutes (12.7 min). This is reduced to only four PVC Ø90 mm pipes in the
nursery raceways and supples 350 l/min or a 100% exchange in 14.5 minutes (Fig.5).
These calculations are based on standard pressure (36 Kpa) and delivery readings at
BIARC and will fluctuate accordingly dependent on those variables and biological
processes, particularly fouling of airlifts (internal) and fouling of end gates reducing the
volume of water in or out. Air is supplied to the raceways by means of a Ø50 mm flexible
delivery line being serviced by the research station’s air delivery system. This system
comprises three aeration blowers, 2 x Wade SR 113 and 1 x Robuschi SRB. The Wade
SR113 is capable of delivering 202 litres/second of air and the Robuschi SRB is capable of
delivering 100 L/S of air. The system has been installed to deliver 502 L/S maximum of air
19
at any one time. The aeration blowers are individually controlled by ABB Variable Speed
Drive Units which are linked to the Central Management System (CMS).
20,000 litre
20,000 litre
3,600 litre Raceway 3,600 litre Raceway
3,600 litre Raceway 3,600 litre Raceway
Figure 3. Nursery and Grow-Out Ra eway Schematic. Blue line indicates air supply
manifold o uplifts.
Figure 4 urned out of water showing aluminium window frames for
housing
raceway
. Raceway upt o
j
tyster mesh screens and a c
oint. close up of end wall and longitudinal section of
20
The CMS monitors temperature, pressure and speed. The signal uses a floating
control algorithm to control the VSD speeds of the blowers. Blowers control to a set point
(adjustable – currently 36Kpa) and shut down at 50Kpa and instigate an alarm. The air
temperature is monitored by the CMS and an alarm raised at a set point of 100°C.
Reticulation water temperature has a set point of 16.6C to maintain the supply air
temperature at 21.6°C. After the air is cooled it is then accepted via a system of ABS and
UPVC pipe work which delivers air to the grow-out pond/reservoir and the rest of the
research site. Blowers are a displacement type and not of compressed air origin.
Figure 5. PVC Nursery Airlift Supply
Grow-out Pond/Reservoir Construction and Management
The 1600m2 (40m x 40m) grow-out pond/reservoir is lined with a 2 mm HDPE liner
with central drainage (Ø150 mm) and monk gate system leading into a large harvest pit.
The pond is 2.4 metres deep at the monk and 2.0 metres deep at the shallow end. Water is
delivered via PVC Ø150 mm pipe and circulated and aerated using 2 x 2hp paddlewheel
aerators. This circulation allows waste material from the raceway to accumulate in the
centre of the pond for easier discharge and to prevent this waste material being introduced
back into the raceway via the airlift system. Pond and raceway water quality is taken twice
daily with a YSI multimeter measuring pH, salinity, DO, secchi depth and temperature.
Critical differences in dissolved oxygen readings between the pond and raceway were the
only discrepancy in water quality measures between the raceways and the grow-out
pond/reservoir. Pond water exchange was regulated using daily water quality measures
and on average 10%/day was exchanged. Pond management required manipulation of
21
phytoplankton blooms to acquire a secchi depth of between 30 and 60 cm using water
exchange and inorganic fertilisation when required. The inorganic fertiliser consisted of
urea, MAP (mono-ammonium phosphate) and potassium nitrate in varying ratios.
Fish are fed twice daily to satiation by hand and then the rest of the calculated ration
added to autofeeders which supply the remaining ration either during the night or very
early in the morning when feeding activity is usually at it’s greatest (Fig.6). Autofeeders
relied on fish surface swimming action (foraging) to activate a suspended pendulum and
activate pellet release. Whiting were fed a Ridley’s Aqua-Feed Native Fish Diet (Slow
Sink) 52:12 (Dust - 3 mm) and 45:10 (4 – 6 mm) and the mulloway were fed a Ridley’s
Aqua-Feed Barramundi Diet (Floating and Sinking) 50:12 and 43:20 (4 - 10 mm). Feeding
activity, weather conditions and water quality parameters where also used to guide
experienced technicians to adjust feed inputs on a daily basis.
Feeding Activity
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Figure 6. Example of Autofeeder Output showing peaks in feeding activity.
22
Figure 7. Plan view of raceway construction
Figure 8. Isometric View of raceway construction.
23
Evaluating Performance of In-Pond Floating Raceways
Sand Whiting
Sand whiting juveniles were produced from hormonally induced broodstock held at
BIARC. Yolk-sac larvae (200,000 or 16/l) were stocked into pre-prepared plankton ponds
and when weaned, the pond was harvested and using a VAKI Bioscanner Fish Counter™ ,
some 17,502 juvenile whiting averaging 5.52 g where stocked into a single nursery
raceway (Trial 1) on the 8th July 2005. Biomass in the raceway was 26.84 kg/m3. The
whiting grew well (Graph 1) and up until harvest on the 4th October 2005 they increased in
average size and biomass to 12.62 g and 51.46 kg/m3 respectively. Specific growth rate
(SGR) was 0.940 and survival for this period was 86%.
On the 4th October 2005, when the biomass had reached 51.46 kg/m3 the single
raceway was harvested and split into two similar nursery raceways (Trial 2). This halved
the biomass in each raceway to 26.5 kg/m3. From the 4th October 2005 until the 15th
December 2005 (11 weeks) the raceways increased in biomass from 26 kg/m³ to 69.24
kg/m³ with a SGR of 1.391
On the 6th January 2006 when the biomass peaked at 69.24 kg/m3 and the fish were
showing signs of stress and dissolved oxygen levels proved difficult to maintain above 4
ppm, the two nursery raceways were harvested and graded such that only the top 50%
grade was returned to the raceways (Trial 3). This lowered the biomass to approximately
45 kg/m3. Whiting by this stage were averaging 33.12 g. The whiting continued to be
grown in the 2 raceways for a further 5 months when biomass peaked at 77.65 kg/m3 and
again the decision was taken due to biological considerations to reduce the biomass by
splitting 3 ways instead of 2. This reduced the biomass to 55 kg/m3 (approx.). This
method of growing fish by manipulating biomass/density and monitoring growth rate, feed
input, general health, critical water quality parameters has given the researchers confidence
to predict whiting will grow well in a nursery raceway at densities up to 70 kg/m3. The
research team had hoped to produce a predictive regression analysis factoring all of these
aforementioned parameters into a raceway management equation but were unable to due to
the ‘noise’ inherent in the data collected.
Whiting appeared to grow equally well at all densities (low and high) up until they
reached the ‘carrying capacity’ of the nursery raceways for this species. Trial 3 utilising
24
the top 50% grade had the lowest SGR and is probably demonstrative of the typical growth
curve for this species of fish. Some of the larger fish were of a size to be reproductively
mature. Further examination of these whiting will confirm this. Fish length, weight and
routine health checks were carried out fortnightly during the trial until May 2006 (autumn)
when mortalities started to appear after handling events. This mortality was subsequently
put down to a secondary Flexibacter columnaris infection caused by excessive handling
and the sudden drop in water temperature. Mortality ceased after handling was reduced or
stopped. Fish recovered without the need for treatment. Whiting were generally well
received in the whole fish (Fig.9) and fillet market. Butterflied and crumbed frozen fish
retailed for more than $20/kg.
Key Points:
1. Nursery raceways were successful in producing whiting in densities up to 70kg/m3.
This equates to a total biomass of approximately 250 kg per unit.
2. The individual weight of whiting grown in nursery raceways increased from 5.52 g
to 88.87 g in 9.5 months
3. FCR for the total nursery production was 1.8:1
4. Whiting biomass at one point increased from 26 kg/m3 to 70 kg/m3 in less than 11
weeks.
5. SGR ranged from 0.520 for Trial 3 to 1.391 for Trial 2
6. Whiting produced in nursery raceways were well received in the market and
retailed whole for $10/kg and fillets up to $24/kg
25
Whiting Growth and Density
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Graph 1. Whiting Growth and Biomass/Density Increase for Nursery Raceways
Table 1. Grow-out Pond/Reservoir Water Quality Summary
G4 DO R1 DO R2 DO R5 DO R6 DO Temp pH Salinity Secchi
Max 12.82 9.30 9.20 9.60 9.40 31.40 9.58 38.80 100
Min 4.32 3.70 3.20 2.80 2.10 15.30 6.65 34.20 25
Figure 9. Whiting from Nursery Raceways for sale
26
Figure 10. Diffuser being laid into the raceways for supplemental aeration.
Mulloway
Mulloway were spawned at a marine finfish hatchery, O’Donohue Sands in New South
Wales. On the 8th February 2005 some 600,000 fertilised eggs were transported in
seawater (10,000/l) via air freight to Brisbane then to BIARC by road. Mulloway eggs
were acclimated and held in incubation tanks for 2 days to hatch. Approx 570,000 yolk-
sac larvae were then stocked into a pre-prepared plankton pond. At harvest, the mulloway
fingerlings were stocked into 30,000 l tanks whilst raceways were still being constructed.
Delays due to injury of a critical staff member meant that construction deadlines were not
met. In the 30,000 tanks the mulloway juveniles suffered ongoing disease issues and
mortality due to Cryptocaryon irritans (White spot) as well as bacterial necrosis of tail
fins. This tail erosion remained permanently disfiguring and can still be seen in market
sized fish (Fig.7). These diseases were treated under veterinary supervision with formalin
followed by freshwater baths and oxytetracyclene (OTC) respectively. A medicated feed
27
was also prescribed. Possible causes were handling stress, poor nutrition and high stocking
densities.
Finally on the 28th September that year the trials were able to commence with what
were now apparently healthy fish. Grow-out raceways were used for the mulloway trials.
These have a working volume of 20,000 litres. Two grow-out raceways were stocked –
Raceway 5 (R5) and Raceway 6 (R6) with graded (by eye) fish. R5 was stocked with 1800
fish weighing on average 171 g. This equated to a biomass of 15.39 kg/m3. R6 was
stocked with 3087 fish weighing on average 96 g. This equated to a biomass of 14.82
kg/m3 – similar to that of R5.
Growth over the year was acceptable (Graph 2) and density in R6 topped 100 kg/m3.
At such time DO levels were approaching critically low levels, as a result feeding activity
was inhibited and there was evidence of compromised fish health. To maintain adequate
DO at this time, supplemental aeration was required through a series of diffusers (Fig.10).
These were simply constructed using bicycle tubes and a lathe tool to puncture up to
10,000 holes per lineal meter. Whilst it remained possible to maintain and grow mulloway
at these densities the SGR dropped from 0.513 to 0.224 over this period. When the
biomass/density of 90kg/m³ was obtained, growth rates stagnated, possible due to lack of
feeding interest, until the density was reduced. Only supplementary aeration maintained
DO levels above critical limits (4.0ppm) as the biomass approached 100kg/m³.
In contrast, Raceway 5 was never allowed to exceed 80 kg/m3 and correspondingly the
SGR was maintained between 0.458 and 0.644. All of the SGR figures given are for the
entire grow-out season and acknowledgement needs to be given to the fact that seasonal
winter temperatures in SE Qld will reduce pond water temperature to <160C. Although not
capable of causing mortality for either species it does create a window of slow to no
growth for a period of approximately 3 months.
Key Points:
1. Grow-out raceways proved successful in producing mulloway at densities up to
100kg per cubic metre. This equates to a total of 2 tonne of fish per raceway.
2. Surface area of the production pond was 1600 m², equating to an equivalent
production rate of more than 30 ton/ha or 3.125 kg/m² of pond production area.
3. Grow-out raceways produced a biomass increase from 15 to 100 kg/m³ in
11months
28
4. Mulloway were grown to market size in less than 10 months - 100g to 500g. Plate
sized fish in 9 months and 170g to 1000g fillet sized fish in 14 months.
5. Average FCR in the grow out raceways was 1.6:1
Mulloway Raceway Growth and Density
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Graph 2. Mulloway Growth and Biomass/Density Increase for Grow-Out Raceways
Table 2. Grow-out Pond/Reservoir Water Quality Summary
G4 DO R1 DO R2 DO R5 DO R6 DO Temp pH Salinity Secchi
Max 12.82 9.30 9.20 9.60 9.40 31.40 9.58 38.80 100
Min 4.32 3.70 3.20 2.80 2.10 15.30 6.65 34.20 25
Marketing
Approximately 1000kg of mulloway were used for market analysis (Fig.11). The fish
ranged in size from 400g through to 1.2kg, with a majority of the fish being less than 1kg.
Two different market avenues were pursued. The first was retail sales to the general public
by a local seafood outlet. Mulloway retailed for approximately $13/kg scaled, head on
gilled and gutted fish, and approximately $16/kg for scaled, skin on fillets. The
appearance and quality of fish was well received however there was continual request for
larger sized fish.
29
The second marketing strategy employed the use of a wholesale fish marketer to
distribute the product into restaurants through Brisbane and surrounding suburbs. Again
the appearance and quality of the fish was well received. Feedback from chefs was in most
cases highly complimentary. The product was deemed to be well suited the Caucasian
community, having a firm white flesh with only a mild flavour. The product was generally
not suited to Asian style preparation. The major restriction encountered in marketing the
fish to restaurants was their size. Fish sold through the wholesaler were 500-900g in
weight. These fish were sold as whole, plate sized fish. There was a general reluctance by
consumers to try plate sized fish. As such there appears to be somewhat limited market for
plate size fish in Brisbane. Feedback from chefs and restaurateurs was that consumers
prefer fish be presented as skinless, boneless fillets. Therefore larger fish (2kg plus) would
be more suitable to the local market and be more likely sustain higher production volume
and may attract better prices. Increased exposure will allow recognition of the quality and
suitably of mulloway to the local market. With the provision of consistent supply and fillet
sized fish (2kg plus) it is believed that mulloway could maintain wholesale prices similar
to that of Barramundi at $8-9/kg. Further research will be conducted to test the market
acceptance of larger fillet sized fish.
Figure 11. Mulloway from Grow-Out Raceways for Sale
30
Economic Analysis/Cost of Production
Based on Australian conditions, our estimations of running costs, capital set up and
depreciation, labour, feed inputs and operating we have determined that raceways are an
economically viable alternative for grow-out production of marine finfish but like all
systems there needs to be an economy of scale and regular supply to good markets. In our
estimation, and based on previous experience with the barramundi industry in Australia, it
is proposed that an aquaculture operation not producing 1000 kg/week for market can
except lower prices, higher costs of production and lower production efficiencies. This
equates to 26 grow-out raceways. This production level would establish an aquaculture
operation in the market place and would demand competitive buying and selling power.
Currently our best estimate for cost of production in raceways is approximately
AUD$8/kg. This will improve over time and compares well with other production systems
but without the large capital input.
Table 3. Routine Labour Requirement for 4 x Nursery and 2 x Grow-out Raceways
(Fig.3)
Procedure Frequency Time (hrs/week)
Water Quality/Pond
Management
2 x Daily 4.25
Feeding 2 x Daily 7.5
Cleaning intake/outlet
screens
2 x weekly x 8 units 4.5
Cleaning uplifts 1 x month x 8 units 2
Total Routine Labour 18.25 hrs/week for 54,400
litre raceway system (Approx
AUD$6/wk/m3)
One of the tangible advantages of raceway production is the lack of initial capital set
up costs for ponds or recirculation operations which frequently run into the 100’s of 1000’s
of $AUD for relatively small operations. Raceways are designed to be self contained
production units requiring only a supply of air and a body of water (of appropriate quality)
to float them in. Construction costs will also reduce as large scale production develops and
raceway size is progressively made larger. This is evident from just our simple
comparison of Grow-Out Raceway construction costs ($130/m3) Vs Nursery raceway
construction costs ($335/m3). Labour costs will also reduce comparatively with larger
system and more economy of scale. The barramundi industry in Qld currently utilises 1
FTE per 16 ton of barramundi produced. Our raceway trial utilised the equivalent of 1
31
FTE for the production of 10 ton. This is an extraordinary achievement in the first year to
come close to other production systems that have been in place for many years.
Grow-out Raceway Construction costs (2 x 20 m3)
Material Cost (AUD$)
Timber $1382.00
HDPE sheets $1723.20
PVC $509.20
Floats $240.00
Fastening materials $365.00
Transfer pump $535.00
Screening material $174.20
HDPE Plumbing $235.40
TOTAL $5164.00 or
$130/m3
Nursery Raceway Construction costs (4 x 3.6 m3)
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Material Cost (AUD$)
Timber $1182.00
HDPE sheets $1723.20
PVC $278.60
Floats $240.00
Fastening materials $300.00
Transfer pump $535.00
Screening material $166.65
HDPE Plumbing $395.00
TOTAL $4820.45 or
$335/m3
Conclusion and Recommendations
Vietnam and Australia (more predominantly Queensland) lacks an efficient and sustainable
nursery and grow-out production system that is simple and practical, cheap to set up and
run and adaptable to the requirements of the species and climate in which the operation is
conducted. Raceways offer a real alternative to the high capital set up and running costs of
coastal pond based system and/or recirculating aquaculture systems (RAS).
Our trials in Australia have demonstrated the validity of a raceway production system for
fingerling and/or grow-out of a number of species and with increased efficiencies and
experience, the researchers believe this type of system will surpass most other production
units in terms of cost of production and flexibility (spatial and species). Further detailed
economic will be conducted at the end of the trial and presented as part of the Final Report.
Experience and results from these grow-out trials will enable the researchers to provide
expertise in systems management, water quality management and waste remediation. All
this work is directly applicable to the larval rearing and nursery focus being investigated in
Vietnam by our project partners.
Acknowledgements
This report uses results of the Project ‘Intensive In-Pond Raceway Production of Marine
Finfish’ CARD VIE 062/04 funded by CARD (Collaboration for Agriculture Research and
Development) program through the Ministry of Agriculture and Rural Development of
Vietnam. The research team would like to thank the Queensland Department of Primary
Industries and Fisheries and our Vietnamese research colleagues ably led by Dr Tung
Hoang (Director, International Centre for Research & Training, Nha Trang University) for
their valuable help and support throughout this project.
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Các file đính kèm theo tài liệu này:
- Báo cáo nghiên cứu khoa học INTENSIVE IN-POND RACEWAY PRODUCTION OF MARINE FINFISH (CARD VIE 062-04) - MILESTONE 2& 4 REPORT.pdf