Item request has been placed! ×
Item request cannot be made. ×
loading  Processing Request

Ammonia removal in freshwater and saltwater systems

Item request has been placed! ×
Item request cannot be made. ×
loading   Processing Request
  • Publication Date:
    September 08, 2020
  • معلومة اضافية
    • Patent Number:
      10766,790
    • Appl. No:
      16/200212
    • Application Filed:
      November 26, 2018
    • نبذة مختصرة :
      An ammonia adsorption product is described which may be used for fresh caught fish and bait. The product may comprise functionalized tectosilicate compound and a buffer. High concentrations of ammonia produced by fish waste can be lethal, even though oxygen availability is rich enough to keep fish breathing. The product is a user-friendly, sustainable, affordable product which is able to extend the life of the fish by safely removing ammonia by an ion-exchange mechanism. This product can convert toxic ammonia into ammonium and uptake ammonium by releasing sodium ions in the water.
    • Inventors:
      Alcantar, Norma A. (Tampa, FL, US); Zhao, Wen (Temple Terrace, FL, US); Ergas, Sarina Joy (Tampa, FL, US)
    • Assignees:
      University of South Florida (Tampa, FL, US)
    • Claim:
      1. A method for producing an ammonia removal agent for saltwater environments, comprising: obtaining a tectosilicate compound wherein the tectosilicate compound is chabazite; functionalizing the tectosilicate compound, comprising soaking the tectosilicate compound in a synthetic saltwater solution for 24 hours and replacing cations in the tectosilicate compound with sodium ions wherein the synthetic saltwater solution consists of: an amount of water; 10.780 g/L of sodium; 0.42 g/L of potassium; 1.32 g/L of magnesium; 19.290 g/L of chloride 0.400 g/L of calcium; 0.200 g/L of bicarbonate; 2.66 g/L of sulfate; and 0.241 g/L of alkalinity; washing the functionalized tectosilicate compound in deionized water; and drying the functionalized tectosilicate compound.
    • Claim:
      2. The method of claim 1 , further comprising washing the tectosilicate compound in deionized water and drying the tectosilicate compound prior to soaking the tectosilicate compound in the synthetic saltwater solution.
    • Claim:
      3. The method of claim 2 , wherein the tectosilicate compound is washed using a shaker table for 24 hours to remove small particles.
    • Claim:
      4. The method of claim 1 , wherein functionalizing the tectosilicate compound increases a percentage of sodium in the tectosilicate compound by at least 30 percent.
    • Claim:
      5. The method of claim 1 , wherein the functionalized tectosilicate compound is dried in an oven at 110° C. for 5 hours.
    • Claim:
      6. The method of claim 1 , wherein the functionalized tectosilicate compound is regenerated by removing adsorbed ammonium ions and replacing them with sodium ions.
    • Claim:
      7. A method for controlling an ammonia level in a water environment, comprising: providing a water environment; providing a functionalized tectosilicate compound, the functionalized tectosilicate compound produced by the steps of: obtaining a tectosilicate compound wherein the tectosilicate compound is chabazite; functionalizing the tectosilicate compound, comprising: soaking the tectosilicate compound in a synthetic freshwater solution or a synthetic saltwater solution; and removing ions from the tectosilicate compound that have a lower cationic affinity than ammonium ions when the synthetic freshwater solution is used or replacing cations in the tectosilicate compound with sodium ions when the synthetic saltwater solution is used; wherein the synthetic freshwater solution consists of: an amount of water; 0.075 g/L of sodium; 0.00312 g/L of potassium; 0.024 g/L of magnesium; 0.193 g/L of chloride 0.043 g/L of calcium; 0.0048 g/L of bicarbonate; 0.096 g/L of sulfate; and 0.310 g/L of alkalinity; wherein the synthetic saltwater solution consists of: an amount of water; 10.780 g/L of sodium; 0.42 g/L of potassium; 1.32 g/L of magnesium; 19.290 g/L of chloride 0.400 g/L of calcium; 0.200 g/L of bicarbonate; 2.66 g/L of sulfate; and 0.241 g/L of alkalinity; washing the functionalized tectosilicate compound in deionized water and then drying the compound; and providing a container for the functionalized tectosilicate compound and a solid pH buffer, the container comprising a porous material to allow liquid to flow through the material; providing for the container of functionalized tectosilicate compound to be placed in a water environment comprising a source of ammonia; buffering the water system to a pH of about 7 and shifting an equilibrium between ammonia and ammonium in the water environment towards ammonium; and adsorbing the ammonium using the functionalized tectosilicate.
    • Claim:
      8. The method of claim 7 , further comprising regenerating the functionalized tectosilicate compound by removing the adsorbed ammonium and replacing with sodium ions.
    • Claim:
      9. The method of claim 7 , further comprising washing the tectosilicate compound in deionized water and drying the tectosilicate compound prior to soaking the tectosilicate compound in the synthetic freshwater solution or the synthetic saltwater solution.
    • Claim:
      10. The method of claim 7 , wherein removing ions from the tectosilicate compound soaked in the synthetic freshwater solution comprises removing sodium ions from the tectosilicate compound.
    • Claim:
      11. The method of claim 10 , wherein functionalizing the tectosilicate compound reduces a percentage of sodium ionically bound to the compound by at least 50 percent.
    • Claim:
      12. The method of claim 7 , wherein the functionalized tectosilicate compound is dried in an oven at 110° C. for 5 hours.
    • Claim:
      13. The method of claim 7 , wherein functionalizing the tectosilicate compound by soaking the tectosilicate compound in the synthetic saltwater solution increases a percentage of sodium in the tectosilicate compound by at least 30 percent.
    • Claim:
      14. A system for removing ammonia from a saltwater environment, comprising: a saltwater environment containing ammonia; a functionalized tectosilicate compound, the functionalized tectosilicate compound produced by the steps of: obtaining a tectosilicate compound wherein the tectosilicate compound is chabazite; functionalizing the tectosilicate compound, comprising soaking the tectosilicate compound in a synthetic saltwater solution and replacing cations in the tectosilicate compound with sodium ions wherein the synthetic saltwater solution consists of: an amount of water; 10.780 g/L of sodium; 0.42 g/L of potassium; 1.32 g/L of magnesium; 19.290 g/L of chloride 0.400 g/L of calcium; 0.200 g/L of bicarbonate; 2.66 g/L of sulfate; and 0.241 g/L of alkalinity; washing the functionalized tectosilicate compound in deionized water and then drying the compound; and a pH buffer, wherein the pH buffer is a phosphate buffer in a solid state wherein an amount of the pH buffer used is such that the pH buffer maintains a pH of 7 in the saltwater environment; and a container holding the functionalized tectosilicate compound and the pH buffer, the container comprising a porous material to allow water to flow through the material; wherein the pH of 7 of the water environment shifts an equilibrium between ammonia and ammonium in the water environment towards ammonium, and the ammonium is adsorbed by the functionalized tectosilicate.
    • Claim:
      15. The system of claim 14 , wherein the functionalized tectosilicate compound is regenerated after use by removing the adsorbed ammonium and replacing with sodium ions.
    • Claim:
      16. The system of claim 14 , wherein functionalizing the tectosilicate compound increases a percentage of sodium in the compound by at least 30 percent.
    • Claim:
      17. The system of claim 14 , wherein the phosphate buffer is Na 2 HPO 4 , NaH 2 PO 4 , or a combination thereof.
    • Patent References Cited:
      5019254 May 1991 Abrevaya
      5489323 February 1996 Yoshida
      5837638 November 1998 Van Der Stok et al.
      8257764 September 2012 Peterson
      10138143 November 2018 Alcantar
      10166528 January 2019 Alcantar
      2018/0194643 July 2018 Litz et al.
      0072147 February 1983
      2192808 January 1988
      2245809 January 1992



























    • Other References:
      Mook, W.T. et al. Removal of total ammonia nitrogen (TAN), nitrate and total organic carbon (TOC) from aquaculture wastewater using electrochemical technology: A review. Desalination 285 (2012) 1-13. cited by applicant
      Zhang, A. and P. Perschbacher. Comarison of the Zeolite Sodium Chabazite and Activated Charcoal for Ammonia Control in Sealed Containers. Asian Fisheries Science 16 (2003): 141-145. cited by applicant
      Bhatnagar, Amit and Mika Sillanpaa. A review of emerging adsorbents for nitrate removal from water. Chemical Engineering Journal 168 (2011) 493-504. cited by applicant
      Bergero, D. et al. Ammonia removal capacity of European natural zeolite tuffs: application to aquaculture waste water. Aquaculture and Fisheries Management 1994, 25, 813-821. cited by applicant
      Zhou, Li et al. Total ammonia nitrogen removal from aqueous solutions by the natural zeolite; mordenite: A laboratory test and experimental study. Aquaculture 432 (2014) 252-257. cited by applicant
      Emadi, H. et al. In vitro Comparison of Zeolite (Clinoptilolite) and Activated Carbon as Ammonia Absorbants in Fish Culture. Naga, The ICLARM Quarterly, vol. 24, Nos. 1 & 2, Jan.-Jun. 2001. cited by applicant
      Lopez-Ruiz, J.L. et al. Zeolites in Marine Nitrogen Transformations. Aquacultural Engineering 13 (1994) 147-152. cited by applicant
      Sing, R.K. et al. Water quality management during transportation of fry of Indian major carps, Catla catla (Hamilton), Labeo rohita (Hamilton) and Cirrhinus mrigala (Hamilton). Aquaculture 235 (2004) 297-302. cited by applicant
      Aponte-Moreales, Veronica et al. Use of Chabazite to Overcome Ammonia Inhibition During Nitrification of High Strength Wastewater. Proceedings of the Water Environment Federation, 2014. 1431-1442.2014. DOI: 10.2175/193864714815941027. cited by applicant
      Ghasemi, Zahra et al. Application of zeolites in aquaculture industry: a review. Reviews in Aquaculture (2018) 10, 75-95. cited by applicant
      Colella, C. Ion exchange equilibria in zeolite minerals. Mineral. Deposita 31, 554-562 (1996). cited by applicant
      Treacy, M.M.J. and J.M. Gibson. The effects of elastic relaxation on transmission electron microscopy studies of thinned compostiion-modulated materials. Journal of Vacuum Science & Technology B: Microelectronics Processing and Phenomena 4, 1458 (1996). DOI: 10.1116/1583473. cited by applicant
      Gendel, Youri and Ori Lahay. A novel approach for ammonia removal from fresh-water recirculated aquaculture systems, comprising ion exchange and electrochemical regeneration. Aquacultural Engineering 52 (2013) 27-38. cited by applicant
      Moussavi, Gholamreza et al. The investigation of mechanism, kinetic and isotherm of ammonia and humic acid co-adsorption onto natural zeolite. Chemical Engineering Journal 171 (2011) 1159-1169. cited by applicant
      Burgess, R.M. et al. Use of Zeolite for Removing Ammonia and Ammonia-Caused Toxicity in Marine Toxicity Identification Evaluations. Arch. Environ. Contain. Toxicol, 2004. 47, 440-447. cited by applicant
      Leyva-Ramos, R. et al. Removal of ammonium from aqueous solution by ion exchange on natural and modified chabazite, Journal of Environmental Management 91 (2010) 2662-2668. cited by applicant
      Alshameri, Aref et al. An investigation into the adsorption removal of ammonium by salt activated Chinese (Hulaodu) natural zeolite: Kinetics, isotherms, and thermodynamics. Journal of the Taiwan Institute of Chemical Engineers 45 (2014) 554-564. cited by applicant
      Karadag, Dogan et al. Removal of ammonium ion from aqueous solution using natural Turkish clinoptilolite. Journal of Hazardous Materials B136 (2006) 604-609. cited by applicant
      Al Dwairi, Reyad A. et al. Potential use of faujasite-phillipsite and phillipsite-chabazite tuff in purification of treated effluent from domestic wastewater treatment plants, Environ Earth Sci (2014) 71:5071-5078. DOI: 10.1007/s12665-013-2911-0. cited by applicant
      Smith, Daniel P. Chabazite Biofilter for Enhanced Stormwater Nitrogen Removal. Water Environment Research Apr. 2011, vol. 83, No. 4, pp. 373-384. cited by applicant
      Non-final office action dated Sep. 19, 2018 for corresponding U.S. Appl. No. 16/023,396. cited by applicant
      Verma, S.S. Wonders of Zeolite. Chemical Business, 2012, 26(2), pp. 10-12. cited by applicant
      Non-final office action dated May 14, 2018 for corresponding U.S. Appl. No. 14/997,793. cited by applicant
      Durborow, R.M. et al. Ammonia in Fish Ponds. Southern Regional Aquaculture Center, 1992, No. 463. cited by applicant
      Final office action dated Sep. 19, 2018 for corresponding U.S. Appl. No. 14/997,793. cited by applicant
      Gyrus, Johnsely S. and G.B. Reddy. Sorption and desorption of ammonium by zeolite: Batch and column studies. Journal of Environmental Science and Health Part A (2011) 46, 408-414. DOI: 10.1080/02773813.2010.542398. cited by applicant
      Miladinovic, N. et al. Ammonia Removal from Saline Wastewater by Ion Exchange. Water, Air, and Soil Pollution: Focus 4: 169-177, 2004. cited by applicant
      Orr, M. et al. What Does That Number Really Mean? Aquarium Water Testing Methods, Results and Interpretation, Sea Scope, 2008, vol. 24, pp. 1-2. cited by applicant
    • Primary Examiner:
      Savage, Matthew O
    • Attorney, Agent or Firm:
      Lawson, Michele L.
      Smith & Hopen, P.A.
    • الرقم المعرف:
      edspgr.10766790