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Fish in the loop:
Exploring RAS
Julie Hansen Bergstedt & Carlos Octavio Letelier-Gordo
Section for Aquaculture
Technical University of Denmark
DTU Aqua
National Institute of Aquatic
Resources
Challenges of the 21st century
2
Challenges:
o Climate change
o Population growth
o Biodiversity
o Water availability
Actions
 Reduce:
o Emissions
o Water utilization
o Land use
Global water availability
3
40% gap in
water supply
compared to
demand in 2030
3% is
freshwater, of
which 1 % is
easily
accessible
* 400 l in RAS
Aquaculture
Consumption
Ornamental
Conservation
4
425 species of
animals, plants, and
algae cultivated
worldwide
22 species account
for >75% of global
production
Global aquaculture
production
5
The largest volume
(89%) of fish is
produced in Asia
SHARE OF AQUACULTURE IN TOTAL FISHERIES AND
AQUACULTURE PRODUCTION BY MAJOR SPECIES
GROUP, 2020
WORLD AQUACULTURE
PRODUCTION, 19912020
Production systems
Cages and pens Open flow Recirculating systems
6
Land-based
Resource utilization
7
 The degree of recirculating is based on make
up- water (MUW) pr. kg feed
 Less CO2 emission, and water and land used
System m3/kg feed
Flow through >50
Re-use RAS 1-50
Conventional RAS 0.1-1
Next gen RAS <0.1
Martins et al. 2010
Increased energy
consumption due
to additional
components
Selection of species
8
Seawater Cubes RAS Unit, 120 m2, 8 tonnes of fish
Danish salmon, RAS in construction, 7500 m2, 1200 tonnes of
fish
 Matching production cost with demand Assessing the
market and project profitability
 Geographical location:
- Availability of electricity, water supply and work force
- Ecology of selected species (cooling systems are
expensive)
9
Requirement of the fish
Water flow
Temperature
Salinity
pH
Light conditions
Dissolved gasses
Stocking density
Feed
composition
Feeding rate
Noise
Tank design
Chemical
stressors
Physical/perceived
stressors
Overall animal health
Growth
Disease resistance
Reproduction
Ineffective utilization of nutrients
Environment
Feed
Water quality
Recirculating aquaculture system
10
 Gas control (O2 and CO2)
 Ammonia (NH3)
 Removal of solids
 Control of pathogens
End-of-pipe-
treatment
Feed and
O2
Solids and metabolic
byproducts
/Ozone
Feed
11
 Standard growth rate (SGR)
 Feed conversion ratio (FCR)
 Digestibility
The majority of the cost is due to feed (46%)
Feed
input
Biomass
produced
1 kg feed
0.9 kg 0.45 kg 0.34 kg
0.24 kg
Feed
Egestion
(faeces)
Ingestion
Growth=
Assimilation-Respiration
Assimilation
Excretion
(NH3)
Respiration
 A large fraction of the animal can be eaten ( 60%)
Metabolism of fish
 Metabolic rate Energy expenditure during a
specific period
 Oxygen consumption (MO2):
 Standard metabolic rate (SMR)
 Maximum metabolic rate (MMR/
MO2max)
 Aerobic scope (AS)
12
0
50
100
150
200
250
300
350
400
450
0 2 4 6 8 10 12 14 16 18 20 22 24
MO
2
(mg
O
2
kg
-1
h
-1
)
Time (h)
MMR
SMR
AS
 Increase in O2 demand after feeding while
the fish are digesting + during increased
activity levels
Automatization
of oxygen
supply !
Controlling gasses
 Oxygen and carbon dioxide consumed and produced by fish
and microbes (biofilter)
 Dissolved oxygen (DO) conc: 80-100%
- Aeration (90-100% of air sat)
- Pure oxygen for supersaturation
 0.5 kg O2 pr kg feed
 CO2: >15 mg/L
 1.4 g pr g O2 consumed
13
200-300%
saturation
Unfed
Tench/doctor fish
(Tinca tinca)
O2 added
CO2
removed
O2 consumption
14
Toxic
ammonia
absent at pH
< 7
 TAN produced 35g/kg feed
 TAN = total ammonia nitrogen
= NH4-N + NH3-N
Ammonia and biofilters
Langenfeld et al. 2021
Nitrifying bacteria
pH
Addition of bicarbonate
to maintain alkalinity and
buffering capacity of the
system
pH of
6.5-8
NH3: >0.2 mg/L
NO2: >0.5 mg/L
NO3: >300 mg/L Summerfelt et al. 2015
Tank design:
 Meet species demand (pelagic of bottom dwelling)
 Circular, square, and octagonal  utilization of space and
strength of design
 Particle residence time
 Self-cleaning effect
15
Solids removal and tank design
Egestion + feed waste
Excretion
(NH3)
Respiration
Feed
Solids
Protein, fat,
carbohydrate
Mechanical filtration
Volume, numbers, life-
stages to
accommodate?
1 kg feed
produces 8 L
of waste
(sludge)
 Total suspended solids (TSS)
TSS= 0.25 * kg feed fed (DM)
16
Control of pathogens
UV
Safe for the fish
Turbidity of water
affects efficiency 
supplement with proper
filtration
Ozone
Efficient oxidation of
organic matter
Flocculation properties
of suspended solids
Hazardous to fish and
people
Chemical
NaCl, H2O2, formalin,
chlorine based
compounds, NaOH,
iodine solutions,
No use of antibiotics
Inlet water Staff Eggs Between batches Outbreaks
Disease in
one part of
the system
will spread to
others !
Dose vs effect
Treating the fish
without harming
the biofilter
Components of RAS
17
Control of pathogens
Gas control
(O2 and CO2)
Removal of metabolic by
products (NH3)
Removal of solids
Ozone
+
Control of
environment
(temp, gasses)
Reduced use of
water
No
escapes/effect
on wild
populations
Waste
treatment
-
High
investment cost
Technological
knowledge
Complex
system
Flow is
key!
End-of-pipe-
treatment
In
Out
18
Thank you
Julie Hansen Bergstedt
juhala@aqua.dtu.dk

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Fish in the Loop: Exploring RAS - Julie Hansen Bergstedt

  • 1. Fish in the loop: Exploring RAS Julie Hansen Bergstedt & Carlos Octavio Letelier-Gordo Section for Aquaculture Technical University of Denmark DTU Aqua National Institute of Aquatic Resources
  • 2. Challenges of the 21st century 2 Challenges: o Climate change o Population growth o Biodiversity o Water availability Actions Reduce: o Emissions o Water utilization o Land use
  • 3. Global water availability 3 40% gap in water supply compared to demand in 2030 3% is freshwater, of which 1 % is easily accessible * 400 l in RAS
  • 4. Aquaculture Consumption Ornamental Conservation 4 425 species of animals, plants, and algae cultivated worldwide 22 species account for >75% of global production
  • 5. Global aquaculture production 5 The largest volume (89%) of fish is produced in Asia SHARE OF AQUACULTURE IN TOTAL FISHERIES AND AQUACULTURE PRODUCTION BY MAJOR SPECIES GROUP, 2020 WORLD AQUACULTURE PRODUCTION, 19912020
  • 6. Production systems Cages and pens Open flow Recirculating systems 6 Land-based
  • 7. Resource utilization 7 The degree of recirculating is based on make up- water (MUW) pr. kg feed Less CO2 emission, and water and land used System m3/kg feed Flow through >50 Re-use RAS 1-50 Conventional RAS 0.1-1 Next gen RAS <0.1 Martins et al. 2010 Increased energy consumption due to additional components
  • 8. Selection of species 8 Seawater Cubes RAS Unit, 120 m2, 8 tonnes of fish Danish salmon, RAS in construction, 7500 m2, 1200 tonnes of fish Matching production cost with demand Assessing the market and project profitability Geographical location: - Availability of electricity, water supply and work force - Ecology of selected species (cooling systems are expensive)
  • 9. 9 Requirement of the fish Water flow Temperature Salinity pH Light conditions Dissolved gasses Stocking density Feed composition Feeding rate Noise Tank design Chemical stressors Physical/perceived stressors Overall animal health Growth Disease resistance Reproduction Ineffective utilization of nutrients Environment Feed Water quality
  • 10. Recirculating aquaculture system 10 Gas control (O2 and CO2) Ammonia (NH3) Removal of solids Control of pathogens End-of-pipe- treatment Feed and O2 Solids and metabolic byproducts /Ozone
  • 11. Feed 11 Standard growth rate (SGR) Feed conversion ratio (FCR) Digestibility The majority of the cost is due to feed (46%) Feed input Biomass produced 1 kg feed 0.9 kg 0.45 kg 0.34 kg 0.24 kg Feed Egestion (faeces) Ingestion Growth= Assimilation-Respiration Assimilation Excretion (NH3) Respiration A large fraction of the animal can be eaten ( 60%)
  • 12. Metabolism of fish Metabolic rate Energy expenditure during a specific period Oxygen consumption (MO2): Standard metabolic rate (SMR) Maximum metabolic rate (MMR/ MO2max) Aerobic scope (AS) 12 0 50 100 150 200 250 300 350 400 450 0 2 4 6 8 10 12 14 16 18 20 22 24 MO 2 (mg O 2 kg -1 h -1 ) Time (h) MMR SMR AS Increase in O2 demand after feeding while the fish are digesting + during increased activity levels Automatization of oxygen supply !
  • 13. Controlling gasses Oxygen and carbon dioxide consumed and produced by fish and microbes (biofilter) Dissolved oxygen (DO) conc: 80-100% - Aeration (90-100% of air sat) - Pure oxygen for supersaturation 0.5 kg O2 pr kg feed CO2: >15 mg/L 1.4 g pr g O2 consumed 13 200-300% saturation Unfed Tench/doctor fish (Tinca tinca) O2 added CO2 removed O2 consumption
  • 14. 14 Toxic ammonia absent at pH < 7 TAN produced 35g/kg feed TAN = total ammonia nitrogen = NH4-N + NH3-N Ammonia and biofilters Langenfeld et al. 2021 Nitrifying bacteria pH Addition of bicarbonate to maintain alkalinity and buffering capacity of the system pH of 6.5-8 NH3: >0.2 mg/L NO2: >0.5 mg/L NO3: >300 mg/L Summerfelt et al. 2015
  • 15. Tank design: Meet species demand (pelagic of bottom dwelling) Circular, square, and octagonal utilization of space and strength of design Particle residence time Self-cleaning effect 15 Solids removal and tank design Egestion + feed waste Excretion (NH3) Respiration Feed Solids Protein, fat, carbohydrate Mechanical filtration Volume, numbers, life- stages to accommodate? 1 kg feed produces 8 L of waste (sludge) Total suspended solids (TSS) TSS= 0.25 * kg feed fed (DM)
  • 16. 16 Control of pathogens UV Safe for the fish Turbidity of water affects efficiency supplement with proper filtration Ozone Efficient oxidation of organic matter Flocculation properties of suspended solids Hazardous to fish and people Chemical NaCl, H2O2, formalin, chlorine based compounds, NaOH, iodine solutions, No use of antibiotics Inlet water Staff Eggs Between batches Outbreaks Disease in one part of the system will spread to others ! Dose vs effect Treating the fish without harming the biofilter
  • 17. Components of RAS 17 Control of pathogens Gas control (O2 and CO2) Removal of metabolic by products (NH3) Removal of solids Ozone + Control of environment (temp, gasses) Reduced use of water No escapes/effect on wild populations Waste treatment - High investment cost Technological knowledge Complex system Flow is key! End-of-pipe- treatment In Out
  • 18. 18 Thank you Julie Hansen Bergstedt juhala@aqua.dtu.dk