Impact of concentrated acid, base and salt pretreatments on the characteristics of natural clinoptilolite and its ammonium uptake from model solution and real effluents
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in: Microporous and Mesoporous Materials, Jahrgang 288.2019, Nr. 1 November, 109553, 01.11.2019.
Publikationen: Beitrag in Fachzeitschrift › Artikel › Forschung › (peer-reviewed)
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T1 - Impact of concentrated acid, base and salt pretreatments on the characteristics of natural clinoptilolite and its ammonium uptake from model solution and real effluents
AU - Stocker, Kristina
AU - Ellersdorfer, Markus
AU - Lechleitner, Andreas
AU - Lubensky, Jan
AU - Raith, Johann
PY - 2019/11/1
Y1 - 2019/11/1
N2 - In this study the influence of highly concentrated reagents (NaCl, 22.36%; HCl, 20%; NaOH, 32%) on the mineralogy (e.g. structure and mineral chemistry) and NH 4 +-exchange capacity of a natural zeolite (clinoptilolite) is investigated. Treatment was executed in packed bed columns and accompanied by liquid and solid analytics (ICP-MS, XRD, EPMA, BET, ion exchange). Ammonium uptake was tested in batch experiments with model solutions using different concentrations of NH 4Cl and real effluents from mechanical sludge dewatering (sludge liquor). It turned out that the Si/Al-ratio of the zeolite minerals measured by EPMA changes to some extent because of dissolution of Si and Al during treatment. Acid treatment leads to a remarkable increase in the specific surface (from 16 to 77 m 2 g -1 after treatment). NH 4 +-exchange isotherms revealed a significant decrease in equilibrium loadings with HCl-treatment and an increase with NaOH-treatment (+25%) at concentrations > 1300 mg NH 4 + L −1 compared to untreated zeolite. At lower concentrations (<1300 mg NH 4 + L −1) treatment with NaCl is best. Basic treatment leads to the formation of an altered outer rim on zeolite particles enriched in Na and depleted in K. Compared to model solutions, ammonium uptake from sludge liquor (712 mg NH 4 + L −1) was significantly lower for NaCl treated zeolite but higher for HCl and NaOH treated samples, probably as a result of the complex composition of real effluents leading to potential cross-interactions that influence NH 4 + ion exchange on treated zeolites.
AB - In this study the influence of highly concentrated reagents (NaCl, 22.36%; HCl, 20%; NaOH, 32%) on the mineralogy (e.g. structure and mineral chemistry) and NH 4 +-exchange capacity of a natural zeolite (clinoptilolite) is investigated. Treatment was executed in packed bed columns and accompanied by liquid and solid analytics (ICP-MS, XRD, EPMA, BET, ion exchange). Ammonium uptake was tested in batch experiments with model solutions using different concentrations of NH 4Cl and real effluents from mechanical sludge dewatering (sludge liquor). It turned out that the Si/Al-ratio of the zeolite minerals measured by EPMA changes to some extent because of dissolution of Si and Al during treatment. Acid treatment leads to a remarkable increase in the specific surface (from 16 to 77 m 2 g -1 after treatment). NH 4 +-exchange isotherms revealed a significant decrease in equilibrium loadings with HCl-treatment and an increase with NaOH-treatment (+25%) at concentrations > 1300 mg NH 4 + L −1 compared to untreated zeolite. At lower concentrations (<1300 mg NH 4 + L −1) treatment with NaCl is best. Basic treatment leads to the formation of an altered outer rim on zeolite particles enriched in Na and depleted in K. Compared to model solutions, ammonium uptake from sludge liquor (712 mg NH 4 + L −1) was significantly lower for NaCl treated zeolite but higher for HCl and NaOH treated samples, probably as a result of the complex composition of real effluents leading to potential cross-interactions that influence NH 4 + ion exchange on treated zeolites.
UR - http://www.scopus.com/inward/record.url?scp=85067605689&partnerID=8YFLogxK
U2 - 10.1016/j.micromeso.2019.06.015
DO - 10.1016/j.micromeso.2019.06.015
M3 - Article
VL - 288.2019
JO - Microporous and Mesoporous Materials
JF - Microporous and Mesoporous Materials
SN - 1387-1811
IS - 1 November
M1 - 109553
ER -