TY - JOUR
T1 - Intensive fish culture at high ammonium and low pH
AU - Eshchar, Micha
AU - Lahav, Ori
AU - Mozes, Noam
AU - Peduel, Adi
AU - Ron, Benny
N1 - Funding Information:
This research was partly funded by the Chief Scientist's Fund, Ministry of Agriculture, Israel.
PY - 2006/5/31
Y1 - 2006/5/31
N2 - Fish excrete two principal toxic metabolites to the water: NH3 and CO2, the former being typically toxic to fish at low (< 0.1 mg N l- 1) concentrations. However, allowing the accumulation of metabolic CO2(aq) results in pH reduction, thereby reducing the fraction of NH3 from TAN. Such operation strategy may allow increasing the design criteria for TAN, which can result in reduced water flow requirements in flow-through systems. In this study, growth parameters of sea bream Sparus aurata grown in high TAN and low pH values, were monitored. TAN toxicity was first tested in 27-l aquariums, where sea bream fingerlings were grown in TAN values of up to 20 mg N l- 1 and pH 6.8, without showing any significant negative effects. Following that, two 100 m3 marine fish-culture tanks were stocked with 84 g fish and supplied with the same daily feed for 250 days. Liquid oxygen enrichment was affected and paddlewheel aerators were used for CO2 stripping. Seawater was supplied to the high TAN experimental system at an average rate of 5.25 m3 (kg feed)- 1 and to a control tank at an average rate of 22.9 m3 (kg feed)-1 (normal flow-through practice). The experimental system included a solids filter, but not a nitrification unit. TAN concentrations measured in the experimental system were much higher than those in the control system (5.44 ± 1.2 mg N l- 1 and 1.34 ± 0.6 mg N l- 1 on average, respectively), however fish growth and fish mortality rates in both systems were statistically identical. The inorganic carbon mass balance differed significantly between the two systems emphasizing the important role of the CO2 stripping device. The choice of stripping device allows controlling the CO2(aq) concentration, which in turn controls the pH value for a given alkalinity value. Such control over the CO2(aq) concentration enables operating the system at relatively high TAN concentrations while maintaining NH3(aq) below the threshold concentration. An aquatic-chemistry model was developed to predict pH value, and consequently CO2(aq) and NH3(aq) concentrations, assuming steady state conditions. Model results were used to determine the minimal makeup water flow-rate that would allow safe operation with regard to the threshold metabolite concentrations. Model results indicated that under the conditions tested, a flow-through system could be operated safely with a ratio as low as 4.4 m3 seawater (kg feed)- 1 with no need for a nitrification biofilter. The implications of growing fish at high TAN concentrations are extensive, the most important being a significant reduction in water treatment costs.
AB - Fish excrete two principal toxic metabolites to the water: NH3 and CO2, the former being typically toxic to fish at low (< 0.1 mg N l- 1) concentrations. However, allowing the accumulation of metabolic CO2(aq) results in pH reduction, thereby reducing the fraction of NH3 from TAN. Such operation strategy may allow increasing the design criteria for TAN, which can result in reduced water flow requirements in flow-through systems. In this study, growth parameters of sea bream Sparus aurata grown in high TAN and low pH values, were monitored. TAN toxicity was first tested in 27-l aquariums, where sea bream fingerlings were grown in TAN values of up to 20 mg N l- 1 and pH 6.8, without showing any significant negative effects. Following that, two 100 m3 marine fish-culture tanks were stocked with 84 g fish and supplied with the same daily feed for 250 days. Liquid oxygen enrichment was affected and paddlewheel aerators were used for CO2 stripping. Seawater was supplied to the high TAN experimental system at an average rate of 5.25 m3 (kg feed)- 1 and to a control tank at an average rate of 22.9 m3 (kg feed)-1 (normal flow-through practice). The experimental system included a solids filter, but not a nitrification unit. TAN concentrations measured in the experimental system were much higher than those in the control system (5.44 ± 1.2 mg N l- 1 and 1.34 ± 0.6 mg N l- 1 on average, respectively), however fish growth and fish mortality rates in both systems were statistically identical. The inorganic carbon mass balance differed significantly between the two systems emphasizing the important role of the CO2 stripping device. The choice of stripping device allows controlling the CO2(aq) concentration, which in turn controls the pH value for a given alkalinity value. Such control over the CO2(aq) concentration enables operating the system at relatively high TAN concentrations while maintaining NH3(aq) below the threshold concentration. An aquatic-chemistry model was developed to predict pH value, and consequently CO2(aq) and NH3(aq) concentrations, assuming steady state conditions. Model results were used to determine the minimal makeup water flow-rate that would allow safe operation with regard to the threshold metabolite concentrations. Model results indicated that under the conditions tested, a flow-through system could be operated safely with a ratio as low as 4.4 m3 seawater (kg feed)- 1 with no need for a nitrification biofilter. The implications of growing fish at high TAN concentrations are extensive, the most important being a significant reduction in water treatment costs.
KW - Ammonia
KW - Carbon dioxide
KW - Flow-through systems
KW - Sea bream
KW - pH control
UR - http://www.scopus.com/inward/record.url?scp=33646881972&partnerID=8YFLogxK
U2 - 10.1016/j.aquaculture.2005.11.034
DO - 10.1016/j.aquaculture.2005.11.034
M3 - Article
AN - SCOPUS:33646881972
SN - 0044-8486
VL - 255
SP - 301
EP - 313
JO - Aquaculture
JF - Aquaculture
IS - 1-4
ER -