Physico-chemical process for removal of nitrogen species from recirculated aquaculture systems
US-2019380313-A1 · Dec 19, 2019 · US
US2017029299A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017029299-A1 |
| Application number | US-201615292863-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 13, 2016 |
| Priority date | Nov 17, 2010 |
| Publication date | Feb 2, 2017 |
| Grant date | — |
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Processes for removing nitrogen species from fresh water or high salinity water recirculated aquaculture systems. The processes are based on physico-chemical treatments which are performed at ambient temperatures and at low pH values thus keeping the total ammonia nitrogen concentrations below a value which is considered detrimental for the growth or survival rate of cultured fish/shrimp.
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1 . A process for removing ammonia from a saline water recirculated aquaculture system (RAS) while maintaining a total ammonia nitrogen (TAN) concentration in the water in said system between 15 and 50 mgN/L, the process comprising the steps of: a. maintaining the pH of the water in the RAS below 7.5 by adding an acid; b. extracting a portion of the water from the RAS; c. oxidizing the ammonia in the portion of the water to nitrogen gas by electrochemical treatment or by breakpoint chlorination in the presence of a solution comprising Cl 2 at concentrations required for attaining breakpoint chlorination; 2 . The process of claim 1 , further comprising the step of recycling at least some of the portion of the water obtained after step (c) back to the RAS. 3 . The process of claim 1 , wherein steps (b) and (c) are performed continuously. 4 . The process of claim 1 , wherein step (b) is performed continuously and step (c) is performed during low cost electricity hours. 5 . The process of claim 1 , wherein the solution comprising Cl 2 is generated in situ by electrooxidation of seawater. 6 . The process of claim 1 , wherein the acid is H 2 SO 4 . 7 . The process of claim 1 , further comprising adding a base during the electrolysis step. 8 . The process of claim 7 , wherein the base is selected from Ca(OH) 2 , CaO, NaOH and KOH. 9 . The process of claim 1 , further comprising stripping of CO 2 wherein stripping of CO 2 comprises the addition of pure oxygen or aeration. 10 . The process of claim 1 , wherein the recirculated aquaculture system (RAS) has a total ammonia nitrogen (TAN) concentration at about 40 mgN/L. 11 . The process of claim 1 , further comprising, repeating steps (a) to (c) in a continuous manner as needed.
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