4.7 Article

Recovery of ammonia from domestic wastewater effluents as liquid fertilizers by integration of natural zeolites and hollow fibre membrane contactors

Journal

SCIENCE OF THE TOTAL ENVIRONMENT
Volume 584, Issue -, Pages 244-251

Publisher

ELSEVIER
DOI: 10.1016/j.scitotenv.2017.01.123

Keywords

Ammonia valorization; Ion-exchange; Natural clinoptilolite; Liquid-liquid membrane contactor; Nitric acid; Phosphoric acid; Liquid fertilizers

Funding

  1. Ministerio de Economia y Competitividad (MINECO) [LIFE12 ENV/ES/000332, CTQ2011-26799, CTM2014-57302-R]
  2. Catalan Government [2014SGR50]
  3. National Council of Science and Technology of Mexico (CONACYT) [213775]

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The integration of up-concentration processes to increase the efficiency of primary sedimentation, as a solution to achieve energy neutral wastewater treatment plants, requires further post-treatment due to the missing ammonium removal stage. This study evaluated the use of zeolites as a post-treatment step, an alternative to the biological removal process. A natural granular clinoptilolite zeolite was evaluated as a sorbent media to remove low levels (up to 100 mg-N/L) of ammonium from treated wastewater using batch and fixed bed columns. After being activated to the Na-form (Z-Na), the granular zeolite shown an ammonium exchange capacity of 29 0.8 mg N-NH4+/g in single ammonium solutions and 23 +/- 0.8 mg N-NH4+/g in treated wastewater simulating up-concentration effluent at pH = 8. The equilibrium removal data were well described by the Langmuir isotherm. The ammonium adsorption into zeolites is a very fast process when compared with polymeric materials (zeolite particle diffusion coefficient around 3 x 10(-12) m(2)/s). Column experiments with solutions containing 100 mg N-NH4+L provide effective sorption and elution rates with concentration factors between 20 and 30 in consecutive operation cydes. The loaded zeolite was regenerated using 2 g NaOH/L solution and the rich ammonium/ammonia concentrates 2-3 g/L in NaOH were used in a liquid-liquid membrane contactor system in a dosed-loop configuration with nitric and phosphoric add as stripping solutions. The ammonia recovery ratio exceeded 98%. Ammonia nitrate and di-ammonium phosphate concentrated solutions reached up to 2-5% wt. of N. (C) 2017 Elsevier B.V. All rights reserved.

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