4.4 Article

Ammonia removal by adsorptive clinoptilolite ceramic membrane: Effect of dosage, isothermal behavior and regeneration process

Journal

KOREAN JOURNAL OF CHEMICAL ENGINEERING
Volume 38, Issue 4, Pages 807-815

Publisher

KOREAN INSTITUTE CHEMICAL ENGINEERS
DOI: 10.1007/s11814-021-0742-3

Keywords

Clinoptilolite; Hollow Fiber Ceramic Membrane (HFCM); Adsorptive Membrane; Ammoniacal-nitrogen Removal; Regeneration

Funding

  1. Ministry of Education Malaysia under Fundamental Research Grant Scheme [R.J130000.7809.5F161]
  2. Ministry of Education Malaysia under Malaysia Research University Network (MRUN) Grant [R.J130000.7851.4L878]
  3. Ministry of Education Malaysia under Higher Institution Centre of Excellence Scheme [R.J090301.7809.4J430]
  4. Universiti Teknologi Malaysia under the Transdisciplinary Research Grant [Q.J130000.3509.05G75]
  5. Universiti Teknologi Malaysia under the UTM High Impact Research (UTMHIR) Grant [Q.J130000.2409.08G34]
  6. Universiti Teknologi Malaysia under the Professional Development Research University (PDRU) Grant [Q.J130000.21A2.05E04]

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The study demonstrates the effective removal of ammoniacal nitrogen from contaminated water using adsorptive hollow fiber ceramic membranes derived from naturally made clinoptilolite. The HFCM exhibits excellent adsorption performance and operational efficiency in removing gaseous ammonia even at trace concentrations, making it a potentially cost-effective and simple technology for ammonia removal from wastewater.
This work investigates the effectiveness of ammoniacal nitrogen (NH4(+)-N) removal from contaminated water by adsorptive hollow fiber ceramic membrane (HFCM) derived from naturally made clinoptilolite. The technological value of this work is the simple mechanism of the adsorptive HFCM in removing gaseous ammonia in water by combining adsorption and separation. To test the technical feasibility of this proposed technology, clinoptilolite HFCM was fabricated via phase inversion-based extrusion/sintering technique and characterized by SEM and water permeation flux. The produced HFCM corresponds to the desired morphology of the asymmetric structure (dense and void formations) with outstanding adsorption performance of NH4(+)-N. The effects of the HFCM's operational parameters on its removal are examined in terms of membrane dosage and isothermal studies. The adsorption isotherm behavior exhibited that the adsorption process fitted the Freundlich isotherm model with outstanding removal performance even at trace concentration of ammonia. The low amount used by HFCM (4.75x10(-4) m(2)) resulted in over 96% ammonia removal, indicating a low cost of adsorption process. The regeneration of saturated HFCM suggests an outstanding recovery of the HFCM for its subsequent use for NH4(+)-N removal. This study also reveals the potential of adsorptive HFCM as a simple and cost-effective technology for ammonia removal from wastewater.

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