Next Article in Journal
Research on the Method of Extracting Water Body Information in Central Asia Based on Google Earth Engine
Next Article in Special Issue
Biological Production and Nitrogen Use Efficiency in a Water-Sharing and Water-Saving System Combining Aquaculture and Vegetable Hydroponic Cultivation
Previous Article in Journal
Correction: Mibarki et al. An Effective Standalone Solar Air Gap Membrane Distillation Plant for Saline Water Desalination: Mathematical Model, Optimization. Water 2023, 15, 1141
Previous Article in Special Issue
Kinetics Modeling for Degradation of Geosmin and 2-Methylisoborneol by Photo-Electrogenerated Radicals
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

Impact of Temperature Reduction from 14 °C to 12 °C in RASs on Atlantic Salmon: Increased Mineral Accumulation in RASs and Enhanced Growth Post-Transfer to Seawater

1
Cargill Aqua Nutrition, Thormøhlens Gate 51, 5006 Bergen, Norway
2
Faculty of Science and Technology (REALTEK), Norwegian University of Life Sciences (NBMU), Universitetstunet 3, 1430 Ås, Norway
*
Author to whom correspondence should be addressed.
Water 2025, 17(6), 803; https://doi.org/10.3390/w17060803
Submission received: 5 February 2025 / Revised: 7 March 2025 / Accepted: 9 March 2025 / Published: 11 March 2025
(This article belongs to the Special Issue Aquaculture Productivity and Environmental Sustainability)

Abstract

:
Robust, healthy, and fast-growing smolt is of high importance for fish farmers as a way of reducing the mortality and production time of Atlantic salmon (Salmo salar) in open sea pens. Lowering the water temperature in flow-through systems (FTSs) compared to recirculating aquaculture systems (RASs) has shown promising results for the growth and health of fish post-transfer to sea; unfortunately, limited information is available on the same parameters in replicated RAS setups. Hence, the current study aimed to compare the performance of Atlantic salmon reared at 12 and 14 °C over a 9-week RAS period and a subsequent 10-week post-transfer period, while also investigating the accumulation pattern of minerals in RASs. The results showed a 100% survival and comparable condition factors and cardiosomatic index (CSI) across both temperatures. During the RAS period, the thermal growth coefficient (TGC) was higher at 12 °C, but body weight gain and feed consumption were lower. No differences in mineral retention or fecal stability were observed. However, the production water accumulated more dissolved phosphorus (DP) and total iron (Fe) at 12 °C. Post-transfer, the TGC remained higher for fish with a rearing history of 12 °C. This fish also had higher body weight gain and feed consumption while exhibiting a lower hepatosomatic index (HSI) and viscerosomatic index (VSI), indicating improved muscle growth. Overall, lower water temperature reduced growth and increased DP and Fe in RASs. However, it improved post-transfer weight gain of muscle tissue, highlighting its benefits for seawater performance.

1. Introduction

Effluents generated from aquaculture production are well known to have potential detrimental effects on water quality and the biodiversity of local fauna [1,2]. This is because aquaculture effluent is rich in nutrient substances like phosphorus (P) and nitrogen (N) and can therefore pose a risk of eutrophication in natural waterbodies when released in excessive amounts [1,2,3]. Due to the potential negative environmental impact, N and P are regulated in the global aquaculture industry, especially for countries in the European Union (EU), where farmers are subject to strict guidelines in terms of effluent regulations on what and how much can be emitted [4,5,6,7]. While N originates from protein digestion in fish [8,9], P, among other things, is a key bone-forming mineral, along with calcium (Ca) and magnesium (Mg), and is thus an essential part of the diet for several aquaculture species [8,10]. The strict regulations on N and P also motivate salmon farmers to invest in technology-intensive farming solutions as a way of reducing and controlling their emissions. One such solution is the recirculating aquaculture system (RAS), which has improved the operational sustainability of fish production by reducing the environmental impact compared to traditional flow-through systems (FTSs) and has generally increased biomass productivity in fish farming [11,12,13]. The multiple benefits of RASs can be credited to the system’s capability of temperature control, reduced water consumption, and its potential for effluent discharge treatment [14,15,16].
The high reuse capability of RASs can cause the production water within the system itself to contain higher levels of total suspended solids (TSS), minerals, metals, nitrogenous compounds, and total gas pressure (TGP) compared to a FTS [17,18,19,20]. This can, in a worst-case scenario, pose a risk to the operation of the RAS and the safety of the fish. In most aquaculture systems, nitrate-N (NO3) concentrations are below 50 mg L−1, but in RASs with low water exchange rates, the concentrations can exceed 400 mg L−1 [21,22]. For the production of salmonids, elevated levels of NO3 in the production water can reduce growth, health, and general performance or increase the mortality of the fish group [23,24,25]. Conversely, the concentration of P in the production water exceeding the recommended levels of 3+ mg L−1 [18] does not necessarily affect fish performance in a negative manner [26]. However, in terms of waste production, elevated P levels increase the risk of eutrophication when combined with elevated N concentrations [1,2,3]. It is important to remember that even in a RAS with a high degree of water reuse, the nutrients that are not removed by the drum filter or foam fractionator, will accumulate in the production water and ultimately be released from the facility in a highly concentrated manner.
While RASs offer operational benefits, the impact of temperature manipulation on fish performance remains understudied. For the production of Atlantic salmon (Salmo salar), the technical system itself will not necessarily affect the performance of the fish post-transfer as long as environmental parameters are kept equal [27]. However, manipulating the temperature can significantly affect the performance of the fish post-transfer to seawater due to its effect on the general biology of the fish, such as heart weight and intestinal fat accumulation [28,29]. Growth rate, feed intake, FCR, and stomach evacuation rate are all affected by temperature [30,31,32]. These parameters are also directly linked to the waste production of fish and, thus, the nutrient release to the production water [33,34,35]. While optimal temperature for freshwater smolts up to 300 g ranges around 14 °C, the optimal temperature for the feed conversion ratio (FCR) is 2 °C lower [31,36]. Since post-transfer seawater performance studies have primarily been conducted by comparing FTSs to RASs, it could be useful for the industry to understand how temperature manipulation within these ranges relates to a pure RAS comparison.
The effect of temperature in RASs has also been documented to strongly correlate with total ammonia nitrogen (TAN) and nitrite (NO2) removal rates in the biofilters, where nitrification rates decrease with decreasing temperature [37,38,39]. Moreover, the biophysical characteristics of feces, such as settling velocities, from channel catfish (Ictalurus punctatus) and bighead carp (Aristichthys nobilis) vary with temperature, affecting how waste disperses and accumulates [40]. Increased particle size and improved fecal stability can be crucial to better encapsulate the particle fraction of N and P compounds until they can be removed by drum filtration [41,42], thus reducing the total emission.
The primary objective of this experiment was, therefore, to compare fish performance of Atlantic salmon reared at a water temperature of 14 °C and a cooler temperature of 12 °C over a 9-week RAS period and a subsequent 10-week post-transfer seawater period in FTSs. A secondary objective was to determine the accumulation pattern of minerals in the production water of the RAS operated at the two water temperatures.

2. Materials and Methods

2.1. Atlantic Salmon and Trial Design

Atlantic salmon post-smolt used in this study were derived from fertilized eggs provided by Aquagen (Atlantic QTL-innOva SHIELD, Aquagen, Kyrksæterøra, Norway) and were hatched and raised on site (Cargill Innovation Center, Dirdal, Norway). The salmon were vaccinated (40–50 g) (Alpha Ject Micro 6, PharmaQ, Norway), pit-tagged, and smoltified (at 70 g using a diet containing salt [EWOS ADAPT FLEX 40, Cargill, Florø, Norway]). On 19 October 2022, a total of 840 post-smolts (240 ± 35 g) were randomly stocked into six RAS units and reared at water temperatures of 12 °C and 14 °C (n = 3). The fish were housed under 24 h light in brackish water (approximately 14‰). The initial biomass density was 33 kg m−3 per RAS tank, and the fish were reared for 9 weeks under the experimental temperature conditions. The fish were transferred into a FTS for a post-transfer period after the 9-week RAS period. During this post-transfer period, 90 fish from each individual RAS unit was distributed into three FTS units, resulting in 30 fish per FTS unit originating from the same RAS tank, or 270 fish in total per temperature treatment (n = 9). This was carried out to ensure a reasonable biomass density and enough fish to sample for the post-transfer period as the fish grew. The post-transfer fish were all reared under identical environmental parameters with temperatures of 9.4 ± 0.6 °C, salinity of 28.8 ± 0.8‰, oxygen saturation in inlet water of 140 ± 13.1%sat, and a light regime with 9 h light and 15 h darkness. The initial biomass density was 16 ± 0.3 kg m−3 per tank, and the fish were reared for 10 weeks under the experimental conditions before the trial was completed. The experimental design is illustrated in Figure 1.

2.2. Production System

This study was conducted in six replicate RASs (Figure 2), each consisting of a total volume of 1500 L, a 1000 L cylindrical rearing tank, a mechanical drum filter (40 μm mesh) with a backwash loop, a three-step biofilter filled with approximately 0.23 m3 of saddle-chip biomedia (Dania plast AS, Mariager, Denmark) in each step, and a pump sump combined with a gas balancing filter (GB filter). Pellet and feces were settled and separated through a swirl separator and collected two to three times a day. An external blower supplied each biofilter chamber with air to maintain stable conditions. CO2 was removed from the GB filter and ventilated out of the systems. Water temperature was regulated with a ceramic heating element and a cooling coil placed in the pump sump, and setpoints were adjusted to achieve target temperatures of 12 °C and 14 °C for the two groups of fish.
The degree of recirculation was roughly 90%, equal to a hydraulic retention time of approximately 10.13 days. All tanks were equipped with flow meters on the seawater and freshwater inlets for constant measurement of water consumption. Make-up water was automatically added to compensate for the wastewater discharged from the drum filter backwash and swirl separator. Alkalinity was maintained at >150 mg L−1 by manually adding sodium bicarbonate (NaHCO3) after wastewater discharge from the drum filter. Dissolved oxygen concentration in the culture tank was operated at approximately 100% saturation throughout the trial. A more detailed description of the RAS can be seen in [26].
Percent daily recirculation and feed per liter of water were calculated as:
Daily recirculation % = 1 Seawater used + Freshwater used Total water volume in the system 100
Feed pr.Litre of new water g L 1 = cumulative feed delivered to tank total new water consumption of tank
The FTS tanks used for the post-transfer period were 1.5 m in diameter and 0.95 m3 in volume.

2.3. Diet and Feeding

A commercial extruded smolt diet (EWOS, Cargill, Bergneset, Norway) suited for Atlantic salmon within the size range and life stage of the current study [43] was fed during the RAS period (Table 1). The water content of the raw material was balanced against the target for the finished diet to ensure that the nutrient contents of the recipe remained accurate and unaffected by variations in the water content; this is considered water balance (Table 1). The feed requirements were determined by internal Cargill feeding tables, and the feed was weighed daily and delivered without interruption by a pre-programmed belt feeder (Alpha Aqua, Esbjerg, Denmark). All salmon were fed to apparent satiation, which was determined to have been reached when excess feed was visually detected at the tank’s bottom. The excess feed, along with feces, was removed gently by a feed collector, designed based on the Guelph system principle [44]. Excess feed and feces were collected twice daily (in the morning at 07:30 and again at 14:30) and manually separated before the uneaten feed was weighed (wet and dry weights).
For the post-transfer period, both groups of salmon were fed a commercial salmon diet containing 42% protein, 32% fat, and 25 MJ kg−1 gross energy (EWOS RAPID HP 500, Cargill, Florø, Norway). The feed was weighed according to the internal Cargill feeding tables and distributed to the tank via a belt feeder (Hølland Teknologi AS, Sandnes, Norway) at an interval of 1.5 h, with 1 h breaks, for a total of four meals during the 9 h light period. Excess feed was removed and weighed from each FTS and recorded every week.

2.4. Water Quality Sampling and Analysis

The measurement and sampling of water quality parameters were performed as described in [26] due to the similarity in the trial designs. The sensor well (Figure 2) provided access to parameters that required monitoring five times a week (Monday to Friday). Water samples were manually collected from each tank and tested for a variety of parameters at different intervals three times a week (Monday, Wednesday, and Friday) and once a week (Monday) (Table 2).
Unionized ammonia (NH3-N) was calculated according to the Henderson–Hasselbach relationship when the water temperature and pH were measured [46]:
N H 3 N = T A N 1 ( 1 + 10 p K a p H )
where the acidic dissociation constant (pKa) was estimated as:
p K a = 0.09018 2729.92 T e m p e r a t u r e , K

2.5. Mineral Sampling and Analysis

To measure mineral accumulation in the RAS, 500 mL of water sample was collected at the start (19 October), middle (16 November), and end (13 December) of the experiment. To understand the distributional pattern of these minerals at different stages of water treatment in the RAS, the water samples were collected directly from the water stream: A. before the fish tank, B. in the swirl separator, C. after the drum filter, and D. after the microparticle filter (Figure 2). The inlet water was collected by removing the flow sensor on the inlet pipe. When the flow sensor was removed, the production water was allowed to flow freely for five seconds before the sample was retrieved. This was performed so that the sample was not contaminated by the sedimented dirt and grime from the opening. The production water was collected in a bucket and returned to the RAS via the swirl separator. Water after the fish tank, after the drum filter, and after the biofilter was collected directly from the water stream by submerging the 500 mL container. After 13 December, turbidity and TSS were also mapped for each water treatment step.
Continuous flow analysis (CFA) was used to determine total phosphorus (TP), dissolved phosphorus (DP), represented as P particles smaller than 0.45 µm, and orthophosphate (PO4-P) in samples by following the NS-EN ISO 15681-2 standard [47]. Bone-forming minerals (Ca and Mg) and sludge classification metals (Fe and Zn) were analyzed by inductively coupled plasma mass spectrometry (ICP-MS) after nitric acid digestion, ensuring that all forms were converted to a measurable solution (SS-EN SS-EN ISO 17294-2:2016 [48]/ISO 15587-2:2002 [49]).

2.6. Fish Sampling, Chemical Composition, and Fecal Stability

All sampled fish, for both the RAS and post-transfer period, were euthanized with a lethal overdose (over 250 mg L−1) of tricaine mesylate (Pharmaq AS, Oslo, Norway) before obtaining the weight and length for each individual, allowing for calculations of the condition factor (K) [50,51], specific growth rate (SGR) [29,52], and thermal growth coefficient (TGC) [53] as per the equations below:
K = 100 weight , g total   length 3 , cm
SGR ( %   day 1 ) = 100 ln final   biomass , g ln ( initial   biomass , g ) time , days
TGC = end   weight , g 1 / 3 ( start   weight , g 1 / 3 ) days   in   sampling     period mean   temperature , ° C 1000
At start of the RAS period, 20 fish in total were sampled for the heart, liver, and viscera. At the end of the RAS period, the heart, liver, and viscera were collected from 10 fish per RAS unit, for a total of 60 fish. For the post-transfer period, the heart, liver, and viscera were collected from 10 fish per FTS tank, for a total of 180. All of the organs were weighed using a precision weight (Ohaus Pioneer PA2102, T.A. Elektronikk AS, Sandnes, Norway) so that the hepatosomatic index (HSI) [54], cardiosomatic index (CSI), and viscerosomatic index (VSI) could be calculated as per the equations below:
HSI = liver weight (g) weight of whole fish (g) 100
CSI = heart weight (g) weight of whole fish (g) 100
VSI = visceral weight (g) weight of whole fish (g) 100
For chemical analysis of the whole body of the fish, 5 fish per RAS unit were collected in the beginning and again at the end of the RAS period. To ensure that the sampled fish were analyzed purely on the content of the body, the fish were dissected to remove stomach and intestinal content (undigested feed). Both the stomach and intestine were scraped clean with a scalpel and then thoroughly cleaned with fresh water before they were placed back into each individual fish. Subsequently, the whole-body samples were frozen at −20 °C until further processing. The frozen fish were then ground down to a fine paste with a Robot-Coupe R7VV industrial grinder (Robot-Coupe, Vincennes, France) before being weighed and dried. The dried paste was then ground again with a coffee grinder to secure a homogenous sample for the chemical analysis. The average retention of the selected minerals in the whole body was estimated as per equation below:
Retention ( % ) = w 2 g     mineral in fish ( g   kg 1 ) 100 w 1 g     mineral in fish ( g   kg 1 ) 100 w 2 ( g ) w 1 ( g )     FCR     mineral in feed ( g   kg 1 ) 100 100
where w1 represents the initial fish weight and w2 is the final fish weight.
Feces from each RAS were retrieved directly from the swirl separator using a 12.5 cm ø mesh stainless steel strainer (Grunwerg, Chesterfield, UK). The retrieved fecal particles were subjected to 5 min of stirring in a Mastersizer 3000 instrument (Malvern Panalytical Ltd., Malvern, UK), where each passage in the instrument reduced the particle size of the fecal sample. A higher fraction of particles larger than 50 µm indicated a higher fecal stability.
The homogenized samples of the whole body and feces were analyzed for minerals with inductively coupled plasma optical emission spectroscopy (ICP-OES) (PerkinElmer, Shelton, CT, USA). The mineral analyses were validated using certified reference materials (Bovine Muscle Certified Reference Material [BOVM-1] for trace metals and European Reference Material [ERM-BB422] for other constituents).

2.7. Statistical Analysis

For the mineral accumulation in RASs, to prevent pseudo-replication issues, generalized mixed linear models (with “log” link) were used to account for the presence of non-independent samples, focusing on the effect of water temperature in RASs on the different minerals tested at different points in time. Every model considered fixed effects for time and temperature as categorical variables (as well as their interaction), along with random effects for the “tank” variable and for the “measurement location”, which was considered to be nested within “tank”. Generalized mixed linear models were also used for the samples collected on a fish basis (TGC, HSI, VSI, and CSI) in RASs and post-transfer. The analysis was performed with a “log” link (the effects were assumed to be multiplicative) for all parameters except the TGC. For the TGC, we utilized a linear approach to better capture its specific relationship with temperature. This was performed by looking at the linear relationship between the cumulative temperature and the difference between the cube roots of the final body weight and the initial body weight.
Water quality parameters, average whole-body retention, and fish performance on a tank basis were analyzed by a one-way ANOVA. The body composition of salmon was tested with a two-way ANOVA, with time and temperature as variables. Due to the lack of fecal samples from the start of the experiment, the chemical analysis of selected minerals in the fecal sample was tested with a one-way ANOVA only for the samples at the end of the experiment to determine differences in the composition. For the analysis of fecal stability, the confidence interval (CI) was determined through simulation and is represented as the 95% CI for the mean of each sample.
Equal variances for the data were investigated with a Levene test (significance level α = 0.05), and post hoc tests were performed either with a Tukey test for pairwise comparisons or with a Dunnett’s test for comparisons against a single reference group (significance level α = 0.05 and highly significant at α = 0.001). The statistical software R (version 4.3.2) and Minitab (20.4, 2021 Minitab, LLC, State College, PA, USA) were used to manage the data.

2.8. Ethical Statement

The experiment adhered to the guidelines and protocols sanctioned by the European Union (EU Council 86/609; D.L. 27 January 1992, no. 116) and the National Guidelines for Animal Care and Welfare issued by the Norwegian Ministry of Education and Research.

3. Results

3.1. Fish Performance

There was no mortality during the entire experimental period. There was significantly higher body weight gain (p < 0.05), length (p < 0.05), and SGR (p < 0.05) for the salmon reared at 14 compared to 12 °C (Table 3) in the RAS period. While the TGC was significantly lower (p < 0.001) in the salmon reared at 14 °C, compared to 12 °C. No differences were observed in the K factor (p = 0.86). At the end of the post-transfer period, salmon with a rearing history of 12 °C had a significantly higher body weight gain (p < 0.05), TGC (p < 0.05) and SGR (p < 0.05) compared to 14 °C. Also, in this period, no significant differences were observed for the K factor (p = 0.94).
Feed consumption was significantly higher for the salmon reared at 14 °C in the RAS period (p < 0.05). Fish reared at 12 °C in the RAS period generally had higher FCR (p = 0.08) compared to fish reared at 14 °C. For the post-transfer period, the tendency shifted to a lower FCR (p = 0.07) for the salmon with a rearing history of 12 °C. However, there was no evidence of difference in FCR either in the RAS or post-transfer period.
In the RAS period, no significant differences were detected for HSI, CSI, or VSI. Post-transfer, there were significant differences in HSI (p < 0.001) and VSI (p < 0.001) between the fish with rearing history of 12 and 14 °C (Figure 3). From the end of the RAS period to the end of the post-transfer period, an increase in HSI was observed for the fish with a rearing history of 14 °C, while VSI increased for both groups.

3.2. Water Quality in RASs

From all the water quality parameters analyzed, significant differences were only observed for the concentration of nitrate (p < 0.05) between the two temperature regimes for the 9-week experimental period in the RAS (Table 4).

3.3. Accumulation of Minerals in RASs

No significant differences were observed in the concentration of any mineral or metal following the flow of the production water through the treatment loop. At the end of the RAS period, significant differences between the temperature regimes were only observed for TP (p < 0.001), DP (p < 0.001), and total Fe (p < 0.001), where the RAS operating with water temperatures of 12 °C accumulated higher concentrations compared to systems with a water temperature of 14 °C (Figure 4). No interactions were found between the time of sampling and location of sampling in the RAS.

3.4. Body Composition of Fish in RASs

The concentrations of selected minerals in the whole body of salmon post-smolt did not differ between temperature regimes (Table 5) from the start to the end of the RAS period. Dry matter, Fe, and Mg concentrations increased between initial and final sampling, while Zn concentrations decreased.
The estimated average retention of selected minerals in the whole body of the salmon did not show evidence of differences between the two fish groups reared at 12 °C and 14 °C (Table 6).

3.5. Chemical Composition of Feces and Fecal Stability in RASs

The chemical composition of feces gathered from the fish reared in RASs showed that only the Mg concentrations were significantly lower for the fish reared at 12 °C; all other minerals and metals were similar between the two temperature regimes (Table 7).
In terms of fecal stability, there was no evidence of differences between the fish groups. The fish reared at 12 °C had a probability of 85.1 ± 2.3% to generate fecal particles smaller than 50 μm vs. 85.5 ± 4.1% for the fish reared at 14 °C.

4. Discussion

Fish reared at 14 °C showed higher growth during the RAS period compared to those at 12 °C, aligning with previous studies on Atlantic salmon [31,36,55,56,57] and findings from the Freshwater Institute in West Virginia [58]. Although the TGC was higher for fish reared at 12 °C, it remained within the target proposed for Atlantic salmon in RASs [59]. The K factor was similar between the two temperature regimes, indicating a comparable slaughter yield [50,51]. Although the FCR was not significantly different between 12 and 14 °C, there was a tendency for higher FCR at lower temperatures (p = 0.08), which was opposite to what was expected [31,36]. Interestingly, the tendency shifted post-transfer to seawater, and the fish with a rearing history of 12 °C ended up with a tendency of lower FCR (p = 0.07) compared to those reared at 14 °C. For the post-transfer period, fish with a rearing history of 12 °C maintained a higher TGC and SGR. This is in line with results showing that lower freshwater temperatures (4–6 °C) before transfer can enhance post-transfer growth in different Atlantic salmon strains, and the pattern in the current study seems to be consistent with studies on compensatory growth [60,61,62]. Additionally, reducing temperatures from 14 to 12 °C during the freshwater period can reduce sexual maturation [58] and improve physiological adaptation to seawater [28,31,61]. Acclimation of fish to post-transfer temperatures is also highlighted as beneficial for growth parameters [31,63,64]. In the current trial, the post-transfer water temperature of 9.4 ± 0.6 °C, being closer to 12 °C, likely gave an advantage to the fish with a freshwater rearing history of 12 over those reared at 14 °C.
Post-transfer, both the HSI and VSI were significantly lower in fish reared at 12 compared to 14 °C. These observations in the RAS, along with the significantly lower HSI post-transfer for the fish reared at a lower temperature, are consistent with a previous study examining fish raised at lower temperatures in a FTS compared to a RAS [28]. Although the current study did not show significant differences in the CSI, it is believed that the small difference in water temperature of 2 °C was not sufficient to inflict a different CSI compared to the previous study, which had a larger difference in water temperature (approximately 5 °C) [28]. The similar post-transfer K factor, combined with a lower VSI for fish with a rearing history of 12 °C, suggests that their weight gain was primarily due to muscle growth. Fish grow faster early in life, with new muscle fibers forming until they reach 40 to 50% of their maximum body length [65]. The growth period where they reach up to approximately 1 kg is thus of high importance due to the recruitment of new muscle fibers [66,67], regardless of smolt type [68]. However, further research is needed to determine if temperature reduction in RASs affects muscle fiber development and fish robustness.
Although the energy requirements for cooling water differ between different RAS setups [69], the RAS units in the current trial generated water temperatures of 20 °C, which needed to be cooled to 12 and 14 °C. Based on the heat capacity of the water, the energy required to cool water an additional 2 °C, from 14 to 12 °C, can be calculated. In the current trial, the total consumption of new water did not differ between the groups (148–145 L day−1). The following equation can be used to determine the energy required to cool 146.5 L day−1, representing the average new water consumption of the tanks in the current study [70]:
Q = m c t
where Q is the heat energy (in joules), m is the mass of the water (in kg), c is the specific heat capacity of water (approximately 4.18 J g°C−1 or 4180 J kg°C−1 [70]), and Δt is the change in temperature (in °C).
Q = 146.5   k g × 4180   J / k g ° C × 2   ° C
To cool the water by an additional 2 °C, 1 224 740 J is required. Using the average price of electricity in Norway for Q3 24 at NOK 1.123 kWh−1, the cost can be calculated as follows [71]:
E n e r g y k W h = 1224740   J 3600000 × N O K   1.123   k W h 1
An extra NOK 0.382 day−1 per RAS unit is needed to cool the water by an additional 2 °C. In relation to the accumulated biomass production of 44.3 kg, this translates to an additional cost of NOK 0.00058 per kg fish produced per day (NOK 0.058 ton fish produced day−1). These calculations are based purely on the effect of the cooling of water, and to relate this to specific RAS productions, energy efficiency, cooling equipment, and additional production time must be considered to adapt the estimate. For the current trial, which only included differences in the water temperature, the extra cost of NOK 0.058 ton fish produced day−1 achieved an approximately 8% increase in body weight gain after 66 days in seawater.
Water samples taken in the RAS showed no differences in compound concentrations between different water treatment steps. Crouse et al. (2022) experienced slightly elevated TSS and nitrate for the salmon reared at 14 compared to 12 °C due to higher feed consumption driven by the elevated temperature, as also shown by previous studies [58,72,73,74]. Similar results were found in the current study, with significantly elevated nitrate at 14 °C. However, the upper recommended limits for nitrate-N (443 mg L−1) and TSS (15 mg L−1) were not exceeded [75,76,77]. Both at 12 and 14 °C, the concentrations of nitrite-N (2.4 and 2.6 mg L−1, respectively) were within the recommended levels reported for salmonids reared in freshwater and seawater (0.1 and 0.5 mg L−1, respectively) [22,78,79]. The concentration of unionized ammonia nitrogen, which has sublethal effect on Atlantic salmon at water concentrations of 10 μg L−1 [80], was also below the lowest recommended level of 12.5 μg L−1 [79]. Since intermediate salinities reduce ammonia toxicity, it is concluded that the concentrations in the current study were well within acceptable levels for salmon [81]. Phosphates play a crucial role in bacterial development, and PO4 can act as a supporting or limiting factor for bacterial growth and activity [3,82,83,84]. The biofilter bacteria, including Nitrosomonas and Nitrobacter, consume PO4 to grow [85]. In the current experiment, a spike in PO4 was observed mid-trial for both temperatures before the levels were reduced again, unlike TP, DP, and dissolved Fe. This could indicate periodic drops in bacterial culture due to the moving bed itself, where biochips regularly collide and detach bacterial pieces that ultimately exit through the recirculation loop [86], potentially also causing variations in TP and DP concentrations. Since the spikes were observed for both temperature regimes and only for PO4, they are more likely to represent the natural development of bacterial cultures [87]. When the biofilter bacteria die, it will take some time to build up the new culture, and in this period, PO4 could increase, as observed in the current trial. Thus, PO4 had the highest fluctuations between the sampling dates of the P components measured in this experiment.
A solution with settling columns was used for fecal removal in the RAS, which is not normal in commercial systems, but the wastewater discharge rates were similar to those of other studies [17,18]. Both the Guelph system and total urine and feces columns are confirmed as suitable methods for fecal collection, ensuring minimal nutrient leakage and damage to the fecal particle [88]. The current experimental system successfully removed larger particles, leaving mainly microparticles to accumulate within the system. This was indicated by analyses that showed no significant difference between TP and DP (NS-EN ISO 15681-2) [47]. Higher TP and DP accumulation at 12 °C were also observed, suggesting that the dissolved fractions will control the accumulation rate in the RAS. This study therefore highlights the challenge of capturing DP in a mechanical filter and supports the suggestions that precipitation or enhanced biological phosphorus removal must be applied to remove DP from the production water [89,90]. Although not proven in the current study, the removal of settleable particles (> 100 μm) [91] may have generated a lack of cake filtration in the drum filter. Accumulated material on the filter (cake) has the potential to provide greater filtration efficiencies than the filter screen alone [92]; subsequently, this lack of cake could have caused a lower removal efficiency of P and particles in general. Drum filters can easily remove particles larger than 30 μm, but smaller microparticles tend to accumulate [77,93,94,95,96]. The material of the drum filter may also affect the removal rates or general accumulation [97]; for example, in the current experiment, polyester was used, but filter media consisting of glass or metal components could generate a different effect within the system. However, this remains unclear and needs to be examined in further studies.
By using an equation to determine concentrations in the outlet of a reuse system [89], it is possible to predict the accumulated concentration measured in RASs compared to what would be expected in a FTS:
C = 1 1 R + R R E
where C is the concentration measured in the outlet or, in our case, the tank, R equals the degree of reuse, and RE equals the removal efficiency.
C = 1 1 0.90 + 0.90 0
C = 10
The removal efficiency is set to zero since the current study suggests that DP will accumulate. With 90% reuse, the concentration of P in the RAS is estimated to be ten times higher than in a FTS. If the current experiment had been conducted in a FTS, the concentrations in the fish tank would have been approximately (4.7 and 3.8 mg L−1)/10 = 0.47 and 0.38 mg L−1 for the 12 and 14 °C regimes, respectively. Cooling the water by an additional 2 °C resulted in a 23.7% increase in DP, which, from an environmental perspective, means that temperature affects how concentrated or dilute the emitted P effluent will be. To illustrate this effect in a practical example, where it is assumed that an average of 18% dietary P is emitted as DP and 52% is emitted as particles in feces [35,98,99,100], reducing the water temperature from 14 to 12 °C could therefore change the emission characteristic to 22.3% DP and 47.7% particle-emitted P, making it harder to collect in sludge treatment. These levels are used as an example, and the availability of P in different raw materials is still the most important factor affecting the composition of the excreted P waste [26]. The elevated DP at 12 °C, compared to 14 °C, may most likely be attributable to a combination of reduced feed consumption and altered P excretion rates, both driven by temperature changes.
In rainbow trout (Oncorhynchus mykiss), the Mg requirement of 330–600 mg kg−1 [43] can be met through the diet or water if water-borne Mg concentrations are at least 46 mg L−1 [101], as seen in low water exchange in brackish RASs [26], similar to that in the current trial. While the Mg requirements can be sufficiently met, the observed 20.5% increase in DP in the current trial is unlikely to cover the total requirement of P for the fish. Estimating water concentrations of P against drinking rates for seawater-adapted salmon (4 mL kg h−1–6.4 mL kg h−1 [102,103]) and assuming, using a simplified example, that a salmon needs approximately 70 days to reach 1 kg, it drinks approximately 6.72–10.75 L of the production water. If the average production water in a RAS contains 5 mg P L−1 (reflecting the 12 °C regime in the current trial), the salmon can only have 33.6–53.7 mg kg−1 growth, which is insignificant compared to the dietary requirement of 6000–10,000 mg kg−1 [43]. To cover the P requirement, a water concentration of 893–930 mg P L−1 would be needed, nearly 200 times higher than that measured in the current trial.
The Ca/P ratio in the salmon was around 1, which was expected and has been confirmed in several studies [104,105,106]. The whole-body composition thus provided an estimated average P retention of 59%, implying a P excretion of 41%. Fecal stability was similar for both temperature treatments, meaning that the amount of feces removed from the system was equal. The feces composition only showed significantly lower Mg for fish reared at 12 °C. The unaffected Zn accumulation in water and in the feces was a positive observation as it indicated that reducing the temperature from 14 to 12 °C did not alter sludge composition. This would be beneficial since the sludge can be graded similarly when used as a fertilizer [107]. However, the 23.7% higher DP concentration in the production water at 12 °C suggests a difference in the nutritional retention of P. Although not significant, P in the feces showed a tendency to be lower (p = 0.1) for fish reared at 12 °C, along with Ca, another bone-forming mineral. It has been proven that a faster growth rate initiated by temperature will promote a more rapid bone development [43,74], meaning the fish will have a higher dietary P requirement at higher temperatures. Exceeding this dietary requirement leads to higher urinary P excretion [108], measurable as DP. While the current trial cannot determine this, future studies with a nutritional trial design and longer RAS period could investigate it. The stable conditions of a RAS can prevent drops in appetite initiated by sudden fluctuations in temperature, thus securing a stable growth rate throughout a production period [109,110,111]. Lowering dietary P to counteract the increased excretion of P when reducing the temperature from 14 to 12 °C while still maintaining growth and health would be beneficial for the industry and environment.

5. Conclusions

This study concludes that rearing fish at 12 °C in a RAS offers several benefits post-transfer to seawater, including a higher TGC and lower VSI and HSI. A reduction from 14 to 12 °C will not negatively affect the Ca/P ratio in Atlantic salmon. Although cooling water from 14 to 12 °C resulted in an 8% higher body weight at the end of post-transfer to seawater, it caused the RAS to accumulate higher levels of DP and total Fe in water at 12 °C, which can increase the effluent emitted if left untreated.

Author Contributions

This research was conceived and designed by V.Ø.F. The experiment, sampling, and preparatory lab work were executed by V.Ø.F. and J.V. Statistical analysis and related graphs produced by V.Ø.F. and T.S. V.Ø.F., J.Ø.H. and O.-I.L. drafted the manuscript. V.Ø.F. and O.-I.L. were involved in interpreting the results. J.Ø.H. and O.-I.L. also supervised the project. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the Research Council of Norway, grant number 329419.

Data Availability Statement

The data presented in this study are available upon request from the corresponding author. The data are not publicly available due to the potential sensitive nature of the information.

Conflicts of Interest

Authors V.Ø.F., J.Ø.H., T.S. and J.V. was employed by the company Cargill Aqua Nutrition. The remaining authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.

List of Abbreviations

Cacalcium
CSIcardiosomatic index
DPdissolved phosphorus
EDXRFenergy-dispersive X-ray fluorescent spectrometer
FCRfeed conversion ratio
Feiron
FTSflow-through system
GBgas balancing
HSIhepatosomatic index
K factorcondition factor
LfNMRlow-field nuclear magnetic resonance
Mgmagnesium
Nnitrogen
NO2nitrite
NO3nitrate
Pphosphorus
PO4orthophosphate
RASrecirculating aquaculture system
SGRspecific growth rate
TANtotal ammonia nitrogen
TGCthermal growth coefficient
TGPtotal gas pressure
TPtotal phosphorus
TSStotal suspended solids
VSIviscerosomatic index
Znzinc

References

  1. Varol, M.; Balcı, M. Characteristics of effluents from trout farms and their impact on water quality and benthic algal assemblages of the receiving stream. Environ. Pollut. 2020, 266, 115101. [Google Scholar] [CrossRef] [PubMed]
  2. Boyd, C.; McNevin, A. Aquaculture, Resource Use, and the Environment; John Wiley & Sons: Hoboken, NJ, USA, 2015. [Google Scholar]
  3. Kim, E.; Yoo, S.; Ro, H.-Y.; Han, H.-J.; Baek, Y.-W.; Eom, I.-C.; Kim, H.-M.; Kim, P.; Choi, K. Aquatic toxicity assessment of phosphate compounds. Environ. Health Toxicol. 2013, 28, e2013002. [Google Scholar] [CrossRef]
  4. Herath, S.; Satoh, S. Environmental impact of phosphorus and nitrogen from aquaculture. In Feed and Feeding Practices in Aquaculture; Elsevier: Amsterdam, The Netherlands, 2015; pp. 369–386. [Google Scholar]
  5. Boyd, C.E. Guidelines for aquaculture effluent management at the farm-level. Aquaculture 2003, 226, 101–112. [Google Scholar] [CrossRef]
  6. Bergheim, A.; Brinker, A. Effluent treatment for flow through systems and European environmental regulations. Aquac. Eng. 2003, 27, 61–77. [Google Scholar] [CrossRef]
  7. Kronvang, B.; Andersen, H.E.; Børgesen, C.; Dalgaard, T.; Larsen, S.E.; Bøgestrand, J.; Blicher-Mathiasen, G. Effects of policy measures implemented in Denmark on nitrogen pollution of the aquatic environment. Environ. Sci. Policy 2008, 11, 144–152. [Google Scholar] [CrossRef]
  8. Hardy, R.W.; Kaushik, S.J. Fish Nutrition; Academic Press: Cambridge, MA, USA, 2021. [Google Scholar]
  9. Kaushik, S.J.; de Oliva Teles, A. Effect of digestible energy on nitrogen and energy balance in rainbow trout. Aquaculture 1985, 50, 89–101. [Google Scholar] [CrossRef]
  10. Helland, S.; Refstie, S.; Espmark, Å.; Hjelde, K.; Baeverfjord, G. Mineral balance and bone formation in fast-growing Atlantic salmon parr (Salmo salar) in response to dissolved metabolic carbon dioxide and restricted dietary phosphorus supply. Aquaculture 2005, 250, 364–376. [Google Scholar] [CrossRef]
  11. True, B.; Johnson, W.; Chen, S. Reducing phosphorus discharge from flow-through aquaculture I: Facility and effluent characterization. Aquac. Eng. 2004, 32, 129–144. [Google Scholar] [CrossRef]
  12. Summerfelt, S.T.; Vinci, B.J. Better management practices for recirculating aquaculture systems. In Environmental Best Management Practices for Aquaculture; John Wiley & Sons: Hoboken, NJ, USA, 2008; pp. 389–426. [Google Scholar] [CrossRef]
  13. Ahmed, N.; Turchini, G.M. Recirculating aquaculture systems (RAS): Environmental solution and climate change adaptation. J. Clean. Prod. 2021, 297, 126604. [Google Scholar] [CrossRef]
  14. Losordo, T.M.; Hobbs, A.O.; DeLong, D.P. The design and operational characteristics of the CP&L/EPRI fish barn: A demonstration of recirculating aquaculture technology. Aquac. Eng. 2000, 22, 3–16. [Google Scholar] [CrossRef]
  15. Roque d’orbcastel, E.; Blancheton, J.-P.; Belaud, A. Water quality and rainbow trout performance in a Danish Model Farm recirculating system: Comparison with a flow through system. Aquac. Eng. 2009, 40, 135–143. [Google Scholar] [CrossRef]
  16. Shnel, N.; Barak, Y.; Ezer, T.; Dafni, Z.; van Rijn, J. Design and performance of a zero-discharge tilapia recirculating system. Aquac. Eng. 2002, 26, 191–203. [Google Scholar] [CrossRef]
  17. Davidson, J.; Good, C.; Welsh, C.; Brazil, B.; Summerfelt, S. Heavy metal and waste metabolite accumulation and their potential effect on rainbow trout performance in a replicated water reuse system operated at low or high system flushing rates. Aquac. Eng. 2009, 41, 136–145. [Google Scholar] [CrossRef]
  18. Davidson, J.; Good, C.; Welsh, C.; Summerfelt, S. The effects of ozone and water exchange rates on water quality and rainbow trout Oncorhynchus mykiss performance in replicated water recirculating systems. Aquac. Eng. 2011, 44, 80–96. [Google Scholar] [CrossRef]
  19. Ebeling, J.M.; Sibrell, P.L.; Ogden, S.R.; Summerfelt, S.T. Evaluation of chemical coagulation–flocculation aids for the removal of suspended solids and phosphorus from intensive recirculating aquaculture effluent discharge. Aquac. Eng. 2003, 29, 23–42. [Google Scholar] [CrossRef]
  20. Martins, C.I.; Pistrin, M.G.; Ende, S.S.; Eding, E.H.; Verreth, J.A. The accumulation of substances in Recirculating Aquaculture Systems (RAS) affects embryonic and larval development in common carp Cyprinus carpio. Aquaculture 2009, 291, 65–73. [Google Scholar] [CrossRef]
  21. Hrubec, T.C.; Smith, S.A.; Robertson, J.L. Nitrate toxicity: A potential problem of recirculating systems. Successes Fail. Commer. Recirc. Aquac. 1996, 1, 41–48. [Google Scholar]
  22. Terjesen, A.B.F.; Rosten, T.W.; Ulgenes, Y.; Henriksen, K.; Aarhus, I.J.; Winther, U. Betydning av vannmiljøet ved produksjon av laksefisk i lukkede systemer i sjø, Water quality requirements for efficient farming of Atlantic salmon in closed systems, In Norwegian, English abstract. VANN 2013, 48, 14–27. [Google Scholar]
  23. Davidson, J.; Good, C.; Welsh, C.; Summerfelt, S.T. Comparing the effects of high vs. low nitrate on the health, performance, and welfare of juvenile rainbow trout Oncorhynchus mykiss within water recirculating aquaculture systems. Aquac. Eng. 2014, 59, 30–40. [Google Scholar] [CrossRef]
  24. Westin, D.T. Nitrate and nitrite toxicity to salmonoid fishes. Progress. Fish-Cult. 1974, 36, 86–89. [Google Scholar] [CrossRef]
  25. Kincheloe, J.W.; Wedemeyer, G.A.; Koch, D.L. Tolerance of developing salmonid eggs and fry to nitrate exposure. Bull. Environ. Contam. Toxicol. 1979, 23, 575–578. [Google Scholar] [CrossRef] [PubMed]
  26. Flo, V.Ø.; Cavrois-Rogacki, T.; Vigen, J.; Gitlesen, T.; Lekang, O.-I. RAS-Designed Diets Result in Lower Accumulation of Nitrogen, Phosphorus, and Zinc in Recirculating Aquaculture System Compared with Traditional Flow-Through Designed Diets. Fishes 2024, 8, 300. [Google Scholar] [CrossRef]
  27. Čižmek, L.; Babić, S.; Strunjak-Perović, I.; Čož-Rakovac, R. Fish liver damage related to the wastewater treatment plant effluents. Environ. Sci. Pollut. Res. Int. 2023, 30, 48739–48768. [Google Scholar] [CrossRef]
  28. Lai, F.; Rønnestad, I.; Budaev, S.; Balseiro, P.; Gelebart, V.; Pedrosa, C.; Stevnebø, A.; Haugarvoll, E.; Korsøen, Ø.J.; Tangen, K.L. Freshwater history influences farmed Atlantic salmon (Salmo salar) performance in seawater. Aquaculture 2024, 586, 740750. [Google Scholar] [CrossRef]
  29. Brett, J.; Groves, T. Physiological energetics. Fish Physiol. 1979, 8, 280–352. [Google Scholar]
  30. Brett, J. Environmental factors and growth. In Fish Physiology; Elsevier: Amsterdam, The Netherlands, 1979; Volume 8, pp. 599–675. [Google Scholar]
  31. Handeland, S.O.; Imsland, A.K.; Stefansson, S.O. The effect of temperature and fish size on growth, feed intake, food conversion efficiency and stomach evacuation rate of Atlantic salmon post-smolts. Aquaculture 2008, 283, 36–42. [Google Scholar] [CrossRef]
  32. Elliot, J.M. The growth rate of brown trout (Salmo trutta L.) fed on maximum rations. J. Anim. Ecol. 1975, 44, 805–821. [Google Scholar] [CrossRef]
  33. Coloso, R.; Basantes, S.; King, K.; Hendrix, M.; Fletcher, J.; Weis, P.; Ferraris, R. Effect of dietary phosphorus and vitamin D3 on phosphorus levels in effluent from the experimental culture of rainbow trout (Oncorhynchus mykiss). Aquaculture 2001, 202, 145–161. [Google Scholar] [CrossRef]
  34. Beamish, F.; Thomas, E. Effects of dietary protein and lipid on nitrogen losses in rainbow trout, Salmo gairdneri. Aquaculture 1984, 41, 359–371. [Google Scholar] [CrossRef]
  35. Wang, X.; Andresen, K.; Handå, A.; Jensen, B.; Reitan, K.I.; Olsen, Y. Chemical composition and release rate of waste discharge from an Atlantic salmon farm with an evaluation of IMTA feasibility. Aquac. Environ. Interact. 2013, 4, 147–162. [Google Scholar] [CrossRef]
  36. Handeland, S.; Arnesen, A.; Stefansson, S. Seawater adaptation and growth of post-smolt Atlantic salmon (Salmo salar) of wild and farmed strains. Aquaculture 2003, 220, 367–384. [Google Scholar] [CrossRef]
  37. Saidu, M.; Hall, S.; Malone, R. Transient temperature effects on biofilters in recirculating systems ammonia removal rates. J. Water Process Eng. 2018, 25, 28–33. [Google Scholar] [CrossRef]
  38. Kinyage, J.P.H.; Pedersen, L.-F. Impact of temperature on ammonium and nitrite removal rates in RAS moving bed biofilters. Aquac. Eng. 2016, 75, 51–55. [Google Scholar] [CrossRef]
  39. Zhu, S.; Chen, S. The impact of temperature on nitrification rate in fixed film biofilters. Aquac. Eng. 2002, 26, 221–237. [Google Scholar] [CrossRef]
  40. Yuan, T.; Wang, Q.; Li, S.; Huang, G.; Zhang, T.; Li, Z.; Liu, J. Assessment of Biophysical Properties of Faecal Pellets from Channel Catfish (Ictalurus punctatus) and Bighead Carp (Aristichthys nobilis). Sustainability 2022, 14, 7201. [Google Scholar] [CrossRef]
  41. Brinker, A. Guar gum in rainbow trout (Oncorhynchus mykiss) feed: The influence of quality and dose on stabilisation of faecal solids. Aquaculture 2007, 267, 315–327. [Google Scholar] [CrossRef]
  42. Brinker, A.; Koppe, W.; Rösch, R. Optimised effluent treatment by stabilised trout faeces. Aquaculture 2005, 249, 125–144. [Google Scholar] [CrossRef]
  43. Lall, S.P. The minerals. In Fish Nutrition, 4th ed.; Elsevier: Amsterdam, The Netherlands, 2022; pp. 469–554. [Google Scholar]
  44. Cho, C.; Slinger, S. Apparent digestibility measurement in feedstuffs for rainbow trout. Finfish Nutr. Fishfeed Technol. 1979, 2, 239–247. [Google Scholar]
  45. NS-EN 872:2005; Water Quality—Determination of Suspended Solids—Method by Filtration Through Glass Fibre Filters 2005. European Committee for Standarization: Brussels, Belgium, 2005.
  46. USEPA. Aquatic Life Ambient Water Quality Criteria for Ammonia-Freshwater; US Environmental Protection Agency: Washington DC, USA, 2013. [Google Scholar]
  47. NS-EN ISO 15681-2:2018; Water Quality—Determination of Orthophosphate and Total Phosphorus Contents by Flow Analysis (FIA and CFA), Part 2: Method by Continuous Flow Analysis (CFA). International Organization for Standarization: Geneva, Switzerland, 2018.
  48. SS-EN ISO 17294-2:2016; Water Quality—Application of Inductively Coupled Plasma Mass Spectrometry (ICP-MS), Part 2: Determination of Selected Elements Including Uranium Isotopes. International Organization for Standarization: Geneva, Switzerland, 2016.
  49. SS-EN ISO 15587-2:2002; Water Quality—Digestion for the Determination of Selected Elements in Water, Part 2: Nitric Acid Digestion. International Organization for Standarization: Geneva, Switzerland, 2002.
  50. Fulton, T. The Rate of Growth of Fishes; 22nd Annual Report of the Fishery Board of Scotland; Fishery Board of Scotland: Edinburgh, Scotland, 1904; pp. 141–241. [Google Scholar]
  51. Ricker, W.E. Computation and interpretation of biological statistics of fish populations. Bull. Fish. Res. Bd. Can. 1975, 191, 1–382. [Google Scholar]
  52. Houde, E.D. Growth rates, rations and cohort consumption of marine fish larvae in relation to prey concentrations. Rapp. P.-V. Réun. Cons. Int. Explor. Mer. 1981, 178, 441–453. [Google Scholar]
  53. Iwama, G.K.; Tautz, A.F. A simple growth model for salmonids in hatcheries. Can. J. Fish. Aquat. Sci. 1981, 38, 649–656. [Google Scholar] [CrossRef]
  54. Chellappa, S.; Huntingford, F.; Strang, R.; Thomson, R. Condition factor and hepatosomatic index as estimates of energy status in male three-spined stickleback. J. Fish Biol. 1995, 47, 775–787. [Google Scholar] [CrossRef]
  55. Solbakken, V.A.; Hansen, T.; Stefansson, S.O. Effects of photoperiod and temperature on growth and parr-smolt transformation in Atlantic salmon (Salmo salar L.) and subsequent performance in seawater. Aquaculture 1994, 121, 13–27. [Google Scholar] [CrossRef]
  56. Handeland, S.; Berge, Å.; Björnsson, B.T.; Lie, Ø.; Stefansson, S. Seawater adaptation by out-of-season Atlantic salmon (Salmo salar L.) smolts at different temperatures. Aquaculture 2000, 181, 377–396. [Google Scholar] [CrossRef]
  57. Austreng, E.; Storebakken, T.; Åsgård, T. Growth rate estimates for cultured Atlantic salmon and rainbow trout. Aquaculture 1987, 60, 157–160. [Google Scholar] [CrossRef]
  58. Crouse, C.; Davidson, J.; Good, C. The effects of two water temperature regimes on Atlantic salmon (Salmo salar) growth performance and maturation in freshwater recirculating aquaculture systems. Aquaculture 2022, 553, 738063. [Google Scholar] [CrossRef]
  59. Thorarensen, H.; Farrell, A.P. The biological requirements for post-smolt Atlantic salmon in closed-containment systems. Aquaculture 2011, 312, 1–14. [Google Scholar] [CrossRef]
  60. Nicieza, A.G.; Metcalfe, N.B. Growth compensation in juvenile Atlantic salmon: Responses to depressed temperature and food availability. Ecology 1997, 78, 2385–2400. [Google Scholar] [CrossRef]
  61. van Rijn, C.A.; Jones, P.L.; Evans, B.S.; Huynh, C.; McCormick, S.D.; Afonso, L.O. Characterization of smoltification in the Tasmanian strain of Atlantic salmon (Salmo salar) in recirculation and flow-through systems. Aquaculture 2020, 516, 734603. [Google Scholar] [CrossRef]
  62. Ali, M.; Nicieza, A.; Wootton, R.J. Compensatory growth in fishes: A response to growth depression. Fish Fish. 2003, 4, 147–190. [Google Scholar] [CrossRef]
  63. Sauter, S.T.; McMillan, J.; Dunham, J. Issue Paper 1: Salmonid Behavior and Water Temperature; EPA-910-D-01-001; Environmental Protection Agency: Seattle, WA, USA, 2001. [Google Scholar]
  64. Torao, M. Effect of water temperature on the feed intake, growth, and feeding efficiency of juvenile chum salmon Oncorhynchus keta after seawater transfer. Aquac. Sci. 2022, 70, 97–106. [Google Scholar] [CrossRef]
  65. Johnston, I.A. Environment and plasticity of myogenesis in teleost fish. J. Exp. Biol. 2006, 209, 2249–2264. [Google Scholar] [CrossRef]
  66. Higgins, P.; Thorpe, J. Hyperplasia and hypertrophy in the growth of skeletal muscle in juvenile Atlantic salmon, Salmo salar L. J. Fish Biol. 1990, 37, 505–519. [Google Scholar] [CrossRef]
  67. Johnston, I.A.; Manthri, S.; Smart, A.; Campbell, P.; Nickell, D.; Alderson, R. Plasticity of muscle fibre number in seawater stages of Atlantic salmon in response to photoperiod manipulation. J. Exp. Biol. 2003, 206, 3425–3435. [Google Scholar] [CrossRef]
  68. Johnsen, C.; Hagen, Ø.; Solberg, C.; Björnsson, B.; Jönsson, E.; Johansen, S.; Bendiksen, E. Seasonal changes in muscle structure and flesh quality of 0+ and 1+ Atlantic salmon (Salmo salar L.): Impact of feeding regime and possible roles of ghrelin. Aquac. Nutr. 2013, 19, 15–34. [Google Scholar] [CrossRef]
  69. Rajesh, M.; Kamalam, B.S.; Sarma, D. Recirculating Aquaculture System for Intensive Fish Farming in Indian Himalayan Region: An Overview. In Fisheries and Aquaculture of the Temperate Himalayas; Springer: Berlin/Heidelberg, Germany, 2023; pp. 173–204. [Google Scholar] [CrossRef]
  70. LibreTexts. Energy and Heat Capacity Calculations. Available online: https://chem.libretexts.org/Courses/Heartland_Community_College/CHEM_120%3A_Fundamentals_of_Chemistry/05%3A_Matter_and_Energy/5.07%3A_Energy_and_Heat_Capacity_Calculations (accessed on 9 January 2025).
  71. Norway, S. Electricity Prices. Available online: https://www.ssb.no/en/energi-og-industri/energi/statistikk/elektrisitetspriser (accessed on 9 January 2025).
  72. Brett, J.; Zala, C. Daily pattern of nitrogen excretion and oxygen consumption of sockeye salmon (Oncorhynchus nerka) under controlled conditions. J. Fish. Board Can. 1975, 32, 2479–2486. [Google Scholar] [CrossRef]
  73. Schumann, M.; Brinker, A. Understanding and managing suspended solids in intensive salmonid aquaculture: A review. Rev. Aquac. 2020, 12, 2109–2139. [Google Scholar] [CrossRef]
  74. Einen, O.; Mørkøre, T. Feeding Theory for Aquaculture; Landbruksforlaget: Oslo, Norway, 1996. [Google Scholar]
  75. Davidson, J.; Good, C.; Williams, C.; Summerfelt, S.T. Evaluating the chronic effects of nitrate on the health and performance of post-smolt Atlantic salmon Salmo salar in freshwater recirculation aquaculture systems. Aquac. Eng. 2017, 79, 1–8. [Google Scholar] [CrossRef]
  76. Good, C.; Davidson, J.; Iwanowicz, L.; Meyer, M.; Dietze, J.; Kolpin, D.W.; Marancik, D.; Birkett, J.; Williams, C.; Summerfelt, S. Investigating the influence of nitrate nitrogen on post-smolt Atlantic salmon Salmo salar reproductive physiology in freshwater recirculation aquaculture systems. Aquac. Eng. 2017, 78, 2–8. [Google Scholar] [CrossRef]
  77. Chen, S.; Timmons, M.B.; Aneshansley, D.J.; Bisogni Jr, J.J. Suspended solids characteristics from recirculating aquacultural systems and design implications. Aquaculture 1993, 112, 143–155. [Google Scholar] [CrossRef]
  78. Wedemeyer, G. Physiology of Fish in Intensive Culture Systems; Springer Science & Business Media: Berlin/Heidelberg, Germany, 1996. [Google Scholar]
  79. Ebeling, J.M.; Timmons, M.B. Recirculating Aquaculture, 5th ed.; Cayuga Aqua Ventures: Ithaca, NY, USA, 2010. [Google Scholar]
  80. Ervik, A.; Ellingsen, H.; Farestveit, E.; Fløysand, R.; Ulriksen, D.; Waagbø, R. The effect of chronic ammonia exposure on growth, gill structure, blood chemistry and catecholamines on Atlantic salmon (Salmo salar) in seawater. Int. Counc. Explor. Sea Comm. Meet F 1987, 1–36. [Google Scholar]
  81. Alabaster, J.; Shurben, D.; Knowles, G. The effect of dissolved oxygen and salinity on the toxicity of ammonia to smolts of salmon, Salmo salar L. J. Fish Biol. 1979, 15, 705–712. [Google Scholar] [CrossRef]
  82. DyhrMaN, S.T.; Ammerman, J.W.; Van Mooy, B.A. Microbes and the marine phosphorus cycle. Oceanography 2007, 20, 110–116. [Google Scholar] [CrossRef]
  83. Heisler, J.; Glibert, P.M.; Burkholder, J.M.; Anderson, D.M.; Cochlan, W.; Dennison, W.C.; Dortch, Q.; Gobler, C.J.; Heil, C.A.; Humphries, E. Eutrophication and harmful algal blooms: A scientific consensus. Harmful Algae 2008, 8, 3–13. [Google Scholar] [CrossRef]
  84. Kroiss, H.; Rechberger, H.; Egle, L. Phosphorus in water quality and waste management. In Integrated Waste Management-Volume II; IntechOpen: London, UK, 2011; pp. 181–214. [Google Scholar]
  85. Meiklejohn, J. Minimum phosphate and magnesium requirements of nitrifying bacteria. Nature 1952, 170, 1131. [Google Scholar] [CrossRef] [PubMed]
  86. Madan, S.; Madan, R.; Hussain, A. Advancement in biological wastewater treatment using hybrid moving bed biofilm reactor (MBBR): A review. Appl. Water Sci. 2022, 12, 141. [Google Scholar] [CrossRef]
  87. Langenheder, S.; Lindström, E.S.; Tranvik, L.J. Structure and function of bacterial communities emerging from different sources under identical conditions. Appl. Environ. Microbiol. 2006, 72, 212–220. [Google Scholar] [CrossRef]
  88. Cho, C.Y. Effect of fecal retrieval timing on digestibility of nutrients in rainbow trout diet with the Guelph and TUF feces collection systems. Nippon Suisan Gakkaishi 1992, 58, 1123–1127. [Google Scholar] [CrossRef]
  89. Lekang, O.-I. Aquaculture Engineering, 3rd ed.; John Wiley & Sons: Hoboken, NJ, USA, 2020. [Google Scholar]
  90. Schleyken, J.; Gumpert, F.; Tränckner, S.; Palm, H.; Tränckner, J. Enhanced chemical recovery of phosphorus from residues of recirculating aquaculture systems (RAS). Int. J. Environ. Sci. Technol. 2024, 21, 3775–3788. [Google Scholar] [CrossRef]
  91. Dolan, E.; Murphy, N.; O’Hehir, M. Factors influencing optimal micro-screen drum filter selection for recirculating aquaculture systems. Aquac. Eng. 2013, 56, 42–50. [Google Scholar] [CrossRef]
  92. Tien, C.; Bai, R. An assessment of the conventional cake filtration theory. Chem. Eng. Sci. 2003, 58, 1323–1336. [Google Scholar] [CrossRef]
  93. Davidson, J.; Summerfelt, S.T. Solids removal from a coldwater recirculating system—Comparison of a swirl separator and a radial-flow settler. Aquac. Eng. 2005, 33, 47–61. [Google Scholar] [CrossRef]
  94. Langer, J.; Efthimiou, S.; Rosenthal, H.; Bronzi, P. Drum filter performance in a recirculating eel culture unit. J. Appl. Ichthyol. 1996, 12, 61–65. [Google Scholar] [CrossRef]
  95. Patterson, R.N.; Watts, K.C.; Timmons, M.B. The power law in particle size analysis for aquacultural facilities. Aquac. Eng. 1999, 19, 259–273. [Google Scholar] [CrossRef]
  96. Pfeiffer, T.J.; Osborn, A.; Davis, M. Particle sieve analysis for determining solids removal efficiency of water treatment components in a recirculating aquaculture system. Aquac. Eng. 2008, 39, 24–29. [Google Scholar] [CrossRef]
  97. Loff, L.G. Filter media, filter rating. In Solid-Liquid Separation; Elsevier: Amsterdam, The Netherlands, 2001; pp. 281–301. [Google Scholar]
  98. Flo, V.Ø. Varieties in Discharge of Nutrient from Land-Based Aquaculture Freshwater Facilities: Flow-Through System vs Recirculating Aquaculture System; Norwegian University of Life Sciences: As, Norway, 2020. [Google Scholar]
  99. Bergheim, A.; Braaten, B. Modell for utslipp fra norske matfiskanlegg til sjø. Rapp. Fra IRIS 2007, 180, 35. [Google Scholar]
  100. Wang, X.; Olsen, L.M.; Reitan, K.I.; Olsen, Y. Discharge of nutrient wastes from salmon farms: Environmental effects, and potential for integrated multi-trophic aquaculture. Aquac. Environ. Interact. 2012, 2, 267–283. [Google Scholar] [CrossRef]
  101. Shearer, K.D.; Åsgård, T. The effect of water-borne magnesium on the dietary magnesium requirement of the rainbow trout (Oncorhynchus mykiss). Fish Physiol. Biochem. 1992, 9, 387–392. [Google Scholar] [CrossRef]
  102. Usher, M.; Talbot, C.; Eddy, F. Drinking in Atlantic salmon smolts transferred to seawater and the relationship between drinking and feeding. Aquaculture 1988, 73, 237–246. [Google Scholar] [CrossRef]
  103. Fuentes, J.; Eddy, F. Drinking in Atlantic salmon presmolts and smolts in response to growth hormone and salinity. Comp. Biochem. Physiol. Part A Physiol. 1997, 117, 487–491. [Google Scholar] [CrossRef]
  104. Aas, T.S.; Åsgård, T.; Ytrestøyl, T. Chemical composition of whole body and fillet of slaughter sized Atlantic salmon (Salmo salar) and rainbow trout (Oncorhynchus mykiss) farmed in Norway in 2020. Aquac. Rep. 2022, 25, 101252. [Google Scholar] [CrossRef]
  105. Baeverfjord, G.; Antony Jesu Prabhu, P.; Fjelldal, P.G.; Albrektsen, S.; Hatlen, B.; Denstadli, V.; Ytteborg, E.; Takle, H.; Lock, E.J.; Berntssen, M.H. Mineral nutrition and bone health in salmonids. Rev. Aquac. 2019, 11, 740–765. [Google Scholar] [CrossRef]
  106. Nordrum, S.; Åsgård, T.; Shearer, K.D.; Arnessen, P. Availability of phosphorus in fish bone meal and inorganic salts to Atlantic salmon (Salmo solar) as determined by retention. Aquaculture 1997, 157, 51–61. [Google Scholar] [CrossRef]
  107. Regulations on Organic Fertilizers. Regulations on Fertilizers Etc. of Organic Origin. §FOR-2003-07-04-951. 2003. Available online: https://lovdata.no/dokument/LTI/forskrift/2003-07-04-951 (accessed on 10 January 2025).
  108. Sugiura, S.H.; Dong, F.M.; Hardy, R.W. A new approach to estimating the minimum dietary requirement of phosphorus for large rainbow trout based on nonfecal excretions of phosphorus and nitrogen. J. Nutr. 2000, 130, 865–872. [Google Scholar] [CrossRef] [PubMed]
  109. Arnekleiv, J.V.; Finstad, A.G.; Rønning, L. Temporal and spatial variation in growth of juvenile Atlantic salmon. J. Fish Biol. 2006, 68, 1062–1076. [Google Scholar] [CrossRef]
  110. Thyholdt, S.B. The importance of temperature in farmed salmon growth: Regional growth functions for Norwegian farmed salmon. Aquac. Econ. Manag. 2014, 18, 189–204. [Google Scholar] [CrossRef]
  111. Finstad, A.G.; Næsje, T.F.; Forseth, T. Seasonal variation in the thermal performance of juvenile Atlantic salmon (Salmo salar). Freshw. Biol. 2004, 49, 1459–1467. [Google Scholar] [CrossRef]
Figure 1. Flowchart of the trial design, illustrating fish groups reared at 12 °C and 14 °C in a RAS period in brackish production water before being transferred to a FTS for a post-transfer period with identical environmental parameters for both groups. Illustrations for light regime: Light (sun) and darkness (moon).
Figure 1. Flowchart of the trial design, illustrating fish groups reared at 12 °C and 14 °C in a RAS period in brackish production water before being transferred to a FTS for a post-transfer period with identical environmental parameters for both groups. Illustrations for light regime: Light (sun) and darkness (moon).
Water 17 00803 g001
Figure 2. Water flow and process design of a replicated Alpha Aqua nanoRAS (Alpha Aqua, Esbjerg, Denmark). The location for the water sampling point is illustrated as follows: A. before the fish tank, B. in the swirl separator, C. after the drum filter, and D. after the microparticle filter. The untreated process water (black arrow), treated process water (blue arrow), backwash water (yellow arrow), and external air blower (purple arrow) are also shown in the figure.
Figure 2. Water flow and process design of a replicated Alpha Aqua nanoRAS (Alpha Aqua, Esbjerg, Denmark). The location for the water sampling point is illustrated as follows: A. before the fish tank, B. in the swirl separator, C. after the drum filter, and D. after the microparticle filter. The untreated process water (black arrow), treated process water (blue arrow), backwash water (yellow arrow), and external air blower (purple arrow) are also shown in the figure.
Water 17 00803 g002
Figure 3. Modelled mean response (with 95% confidence interval) of the (a) hepatosomatic index (HSI), (b) cardiosomatic index (CSI), and (c) viscerosomatic index (VSI) in Atlantic salmon (Salmo salar) post-smolts reared at 12 °C and 14 °C in RASs and after the post-transfer stage.
Figure 3. Modelled mean response (with 95% confidence interval) of the (a) hepatosomatic index (HSI), (b) cardiosomatic index (CSI), and (c) viscerosomatic index (VSI) in Atlantic salmon (Salmo salar) post-smolts reared at 12 °C and 14 °C in RASs and after the post-transfer stage.
Water 17 00803 g003aWater 17 00803 g003b
Figure 4. Modelled mean response (95% confidence interval) over different days (0, 28, and 55) for accumulated minerals: (a) total phosphorus (TP), (b) dissolved phosphorus (DP), (c) orthophosphate (PO4), (d) calcium (Ca), (e) magnesium (Mg), (f) total zinc (Zn), (g) dissolved zinc (Zn), (h) total iron (Fe), and (i) dissolved iron (Fe) in water from RASs with Atlantic salmon (Salmo salar) post-smolts reared at 12 °C (red) and 14 °C (turquoise) (n = 3).
Figure 4. Modelled mean response (95% confidence interval) over different days (0, 28, and 55) for accumulated minerals: (a) total phosphorus (TP), (b) dissolved phosphorus (DP), (c) orthophosphate (PO4), (d) calcium (Ca), (e) magnesium (Mg), (f) total zinc (Zn), (g) dissolved zinc (Zn), (h) total iron (Fe), and (i) dissolved iron (Fe) in water from RASs with Atlantic salmon (Salmo salar) post-smolts reared at 12 °C (red) and 14 °C (turquoise) (n = 3).
Water 17 00803 g004aWater 17 00803 g004bWater 17 00803 g004c
Table 1. Formulation of ingredients and chemical analysis of the content for the commercial diet.
Table 1. Formulation of ingredients and chemical analysis of the content for the commercial diet.
ParameterDiet
Ingredient (%)
Fish meal (LT94)27.9
Plant ingredients43.5
Marine oils10.8
Plant oils16.9
Micro ingredients *5.0
Water balance −4.1
Composition (%, “as-is basis”)Method of analysis
Protein40.6Elementar Rapid Max N system (Dumas principle) (Elementar Analysesysteme GmbH, Langenselbold, Germany)
Fat34.7NMR Analyzer Bruker minispec mq10 system (Bruker, Billerica, MA, USA) LfNMR scan
Moisture3.9Leco TGA 701 analyzer (Leco, Geleen, The Netherlands)
Ash6.7
Gross energy (MJ kg−1)25.4Leco AC 600 gross energy bomb calorimetry system (Leco, Geleen, The Netherlands)
Carbohydrate a18.0na
Minerals (g kg−1, “as-is basis”)
Phosphorus9.3PUMA s2 EDXRF (Bruker, MA, USA)
Calcium10.1
Zinc 0.18
Iron0.22
Notes: * Vitamins, minerals, and amino acids. a Carbohydrate = 100 − Ash − Protein − Fat. NMR: nuclear magnetic resonance. LfNMR: low-field nuclear magnetic resonance. EDXRF: energy-dispersive X-ray fluorescent spectrometer.
Table 2. Description and frequency of testing for each water quality parameter monitored and sampled in RASs stoked with Atlantic salmon (Salmo salar).
Table 2. Description and frequency of testing for each water quality parameter monitored and sampled in RASs stoked with Atlantic salmon (Salmo salar).
ParameterMethod of AnalysisFrequency
TemperatureMulti-parameter portable meter WTW multi 3620 IDS (Xylem Analytics, Mainz, Germany)5 times a week
pH5 times a week
Salinity5 times a week
Oxygen5 times a week
CO2Franatech dissolved CO2 sensor HR (Franatech AS, Oslo, Norway)5 times a week
TANSpectroquant cell test kits (Merck, Darmstadt, Germany) Spectroquant Prove 300 (Merck, Darmstadt, Germany)3 times a week
NO23 times a week
NO33 times a week
Alkalinity3 times a week
TurbidityWTW Turb750 IR (Xylem Analytics, Mainz, Germany)3 times a week
TSSStandard methods NS-EN872:2005 [45]1 time a week
TGPOxyguard Handy Polaris TGP (Oxyguard, Farum, Denmark)1 time a week
Notes: TAN: total ammonia nitrogen; NO2: nitrite; NO3: nitrate; TSS: total suspended solids; and TGP: total gas pressure.
Table 3. Fish performance parameters in Atlantic salmon (Salmo salar) post-smolts reared at 12 °C and 14 °C in RASs and after the post-transfer stage. Data are expressed as averages on a tank basis ± SD for each temperature regime in RASs and for post-transfer. Data were analyzed by a one-way ANOVA (p < 0.05), with weight, length, and K factor per tank and with thermal growth coefficient, specific growth rate, feed consumption, feed conversion ratio, and mortality per temperature regime.
Table 3. Fish performance parameters in Atlantic salmon (Salmo salar) post-smolts reared at 12 °C and 14 °C in RASs and after the post-transfer stage. Data are expressed as averages on a tank basis ± SD for each temperature regime in RASs and for post-transfer. Data were analyzed by a one-way ANOVA (p < 0.05), with weight, length, and K factor per tank and with thermal growth coefficient, specific growth rate, feed consumption, feed conversion ratio, and mortality per temperature regime.
RASPost-Transfer
Initial weight (g)
12 °C239 ± 3563 ± 12
14 °C241 ± 2570 ± 11
Final weight (g)
12 °C554 ± 9 *1197 ± 30
14 °C575 ± 6 *1156 ± 53
Body weight gain (g)
12 °C315 ± 7 *634 ± 29 *
14 °C334 ± 6 *586 ± 50 *
Length (cm)
12 °C34 ± 0.2 *43 ± 0.44
14 °C35 ± 0.03 *42 ± 0.77
K factor
12 °C1.39 ± 0.011.51 ± 0.02
14 °C1.39 ± 0.021.51 ± 0.03
Feed consumption (kg)
12 °C35.4 ± 0.3 *16.4 ± 0.7 *
14 °C36.1 ± 0.1 *15.0 ± 1.1 *
Feed conversion ratio
12 °C0.80 ± 0.010.84 ± 0.02
14 °C0.77 ± 0.010.86 ± 0.03
Thermal growth coefficient
12 °C2.99 ± 0.05 **3.85 ± 0.2 *
14 °C2.67 ± 0.04 **3.53 ± 0.3 *
Specific growth rate
12 °C1.50 ± 0.03 *1.09 ± 0.04 *
14 °C1.55 ± 0.02 *1.02 ± 0.06 *
Notes: Significance levels: * p < 0.05 and ** p < 0.001.
Table 4. Water quality measures in brackish recirculating aquaculture systems operated at water temperatures of 12 °C and 14 °C for 9 weeks. Data are expressed as averages for the trial period ± SD (n = 3). Data were analyzed by a one-way ANOVA (p < 0.05).
Table 4. Water quality measures in brackish recirculating aquaculture systems operated at water temperatures of 12 °C and 14 °C for 9 weeks. Data are expressed as averages for the trial period ± SD (n = 3). Data were analyzed by a one-way ANOVA (p < 0.05).
12 °C14 °C
pH7.6 ± 0.057.7 ± 0.02
Salinity (ppt)14.6 ± 0.1314.5 ± 0.19
Dissolved oxygen (ppm)8.70 ± 0.048.88 ± 0.16
CO2 (mg L−1)8.7 ± 0.198.6 ± 0.20
Alkalinity (mg L−1)159 ± 4.24151 ± 3.25
TAN (mg L−1)0.6 ± 0.110.5 ± 0.04
Nitrite—Nitrogen (mg L−1)2.4 ± 0.712.6 ± 0.13
Nitrate—Nitrogen (mg L−1)55 ± 0.61 *62 ± 2.98 *
Unionized ammonia—Nitrogen (μg L−1)5.5 ± 1.66.0 ± 0.1
TSS (mg L−1)8.31 ± 1.068.70 ± 0.60
Turbidity (NTU)1.1 ± 0.400.9 ± 0.18
TGP (<102%)96.0 ± 0.6795.5 ± 1.78
Freshwater consumption (L day−1)94.1 ± 8.8792.8 ± 8.06
Seawater consumption (L day−1)53.9 ± 5.6052.2 ± 4.13
New water consumption (L day−1)148 ± 13.3145 ± 11.9
Total feed per liter of new water (g L−1)5.3 ± 0.165.3 ± 0.50
Recirculation degree (% day−1)90 ± 0.9190 ± 0.81
Notes: TAN: total ammonia nitrogen; TSS: total suspended solids; and TGP: total gas pressure. * Significant at p < 0.05.
Table 5. Chemical analysis of dry matter and selected minerals in the whole body of Atlantic salmon reared in RASs at 12 °C and 14 °C measured at the start and end of the RAS period (19 October to 13 December). The average initial weight was 240 ± 35 g, and the final weight was 554 ± 9 g at 12 °C and 575 ± 5 g at 14 °C. Data were analyzed by a two-way ANOVA (time, temperature, and time × temperature [interaction]) and are given as mean ± SD (n = 3) in wet weight (as-is).
Table 5. Chemical analysis of dry matter and selected minerals in the whole body of Atlantic salmon reared in RASs at 12 °C and 14 °C measured at the start and end of the RAS period (19 October to 13 December). The average initial weight was 240 ± 35 g, and the final weight was 554 ± 9 g at 12 °C and 575 ± 5 g at 14 °C. Data were analyzed by a two-way ANOVA (time, temperature, and time × temperature [interaction]) and are given as mean ± SD (n = 3) in wet weight (as-is).
p-Value
InitialFinalTimeTemperatureInteraction
Dry matter (%)
12 °C31.2 ± 0.636.3 ± 0.2
14 °C31.6 ± 0.236.3 ± 0.7<0.0010.5150.510
Calcium (g kg−1)
12 °C4.4 ± 0.14.0 ± 0.3
14 °C4.6 ± 0.34.4 ± 0.30.1230.1080.659
Iron (mg kg−1)
12 °C8.2 ± 0.211.2 ± 0.2
14 °C8.9 ± 0.512.3 ± 3.80.0200.4540.858
Magnesium (mg kg−1)
12 °C294 ± 13320 ± 22
14 °C302 ± 5321 ± 70.0190.5930.714
Phosphorus (g kg−1)
12 °C4.4 ± 0.24.4 ± 0.3
14 °C4.5 ± 0.14.4 ± 0.10.3950.4840.768
Zinc (mg kg−1)
12 °C44 ± 141 ± 3
14 °C47 ± 141 ± 10.0040.2840.080
Table 6. Estimated average retention of selected minerals in the whole body of Atlantic salmon reared in RASs at 12 °C and 14 °C + SD (n = 3). The average initial weight was 240 ± 35 g, and the final weight was 554 ± 9 g at 12 °C and 575 ± 5 g at 14 °C. Data were analyzed by a one-way ANOVA.
Table 6. Estimated average retention of selected minerals in the whole body of Atlantic salmon reared in RASs at 12 °C and 14 °C + SD (n = 3). The average initial weight was 240 ± 35 g, and the final weight was 554 ± 9 g at 12 °C and 575 ± 5 g at 14 °C. Data were analyzed by a one-way ANOVA.
Average Whole-Body Retention (%)p-Value
Calcium
12 °C47 ± 6
14 °C55 ± 50.179
Iron
12 °C8 ± 0.3
14 °C9 ± 40.730
Phosphorus
12 °C58 ± 9
14 °C60 ± 20.695
Zinc
12 °C28 ± 4
14 °C26 ± 10.438
Table 7. Chemical analysis of selected minerals (mg kg−1) in feces of Atlantic salmon reared in RASs at 12 °C and 14 °C from 19 October to 13 December. The average initial weight was 240 ± 35 g, and the final weight was 554 ± 9 g at 12 °C and 575 ± 5 g at 14 °C. Data were analyzed by a one-way ANOVA and are given as mean ± SD (n = 3).
Table 7. Chemical analysis of selected minerals (mg kg−1) in feces of Atlantic salmon reared in RASs at 12 °C and 14 °C from 19 October to 13 December. The average initial weight was 240 ± 35 g, and the final weight was 554 ± 9 g at 12 °C and 575 ± 5 g at 14 °C. Data were analyzed by a one-way ANOVA and are given as mean ± SD (n = 3).
G kg−1p-Value
Calcium
12 °C44.7 ± 2.08
14 °C46.7 ± 2.080.305
Iron
12 °C0.83 ± 0.02
14 °C0.84 ± 0.020.588
Magnesium
12 °C5.27 ± 0.32
14 °C6.83 ± 0.060.001 *
Phosphorus
12 °C24.3 ± 1.53
14 °C26.7 ± 1.150.102
Zinc
12 °C0.55 ± 0.01
14 °C0.55 ± 0.020.768
Notes: * Significant difference between temperatures (p < 0.05).
Disclaimer/Publisher’s Note: The statements, opinions and data contained in all publications are solely those of the individual author(s) and contributor(s) and not of MDPI and/or the editor(s). MDPI and/or the editor(s) disclaim responsibility for any injury to people or property resulting from any ideas, methods, instructions or products referred to in the content.

Share and Cite

MDPI and ACS Style

Flo, V.Ø.; Hansen, J.Ø.; Silva, T.; Vigen, J.; Lekang, O.-I. Impact of Temperature Reduction from 14 °C to 12 °C in RASs on Atlantic Salmon: Increased Mineral Accumulation in RASs and Enhanced Growth Post-Transfer to Seawater. Water 2025, 17, 803. https://doi.org/10.3390/w17060803

AMA Style

Flo VØ, Hansen JØ, Silva T, Vigen J, Lekang O-I. Impact of Temperature Reduction from 14 °C to 12 °C in RASs on Atlantic Salmon: Increased Mineral Accumulation in RASs and Enhanced Growth Post-Transfer to Seawater. Water. 2025; 17(6):803. https://doi.org/10.3390/w17060803

Chicago/Turabian Style

Flo, Vegard Øvstetun, Jon Øvrum Hansen, Tomé Silva, Jannicke Vigen, and Odd-Ivar Lekang. 2025. "Impact of Temperature Reduction from 14 °C to 12 °C in RASs on Atlantic Salmon: Increased Mineral Accumulation in RASs and Enhanced Growth Post-Transfer to Seawater" Water 17, no. 6: 803. https://doi.org/10.3390/w17060803

APA Style

Flo, V. Ø., Hansen, J. Ø., Silva, T., Vigen, J., & Lekang, O.-I. (2025). Impact of Temperature Reduction from 14 °C to 12 °C in RASs on Atlantic Salmon: Increased Mineral Accumulation in RASs and Enhanced Growth Post-Transfer to Seawater. Water, 17(6), 803. https://doi.org/10.3390/w17060803

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop