US2017029299A1PendingUtilityA1

Physico-chemical process for removal of nitrogen species from recirculated aquaculture systems

Assignee: TECHNION RES & DEV FOUNDATIONPriority: Nov 17, 2010Filed: Oct 13, 2016Published: Feb 2, 2017
Est. expiryNov 17, 2030(~4.3 yrs left)· nominal 20-yr term from priority
A01K 63/04B01J 49/50Y02A40/81B01J 49/53C02F 1/42C02F 2209/14C02F 2101/105C02F 1/4674B01J 39/04C02F 1/20B01D 2256/10C02F 1/66A01K 61/10B01J 49/00C02F 2101/16C02F 2303/16A01K 61/00B01J 39/18C02F 1/46C02F 1/586C02F 2209/06C02F 2209/16B01J 49/0069
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Claims

Abstract

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.

Claims

exact text as granted — not AI-modified
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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