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Salinity Mitigation for Potash Mine Sites: Synergistic Cation and Anion Removal Using a Dual-Adsorbent

Date

2017-01-12

Journal Title

Journal ISSN

Volume Title

Publisher

ORCID

0000-0003-0156-9197

Type

Thesis

Degree Level

Masters

Abstract

Potash (KCl) mining generates large quantities of tailings and brine which can impact proximate aquifers, elevating the concentrations of Na+, K+, and Cl-. To desalinate brine-impacted groundwater near potash mines and other inland locations, two adsorbents were sequentially applied: (1) calcined layered double hydroxide (CLDH), to adsorb anions, divalent cations, and transiently raise the pH; and (2) acid-treated clinoptilolite zeolite, to adsorb monovalent cations and neutralize the effluent pH. To evaluate this dual-adsorbent process, equilibrium adsorption experiments were conducted and the adsorbents were characterized through X-ray diffraction, X-ray florescence, porosimetry, scanning electron microscopy, and synchrotron-based scanning transmission X-ray microscopy. Using synthetic NaCl solution, the Langmuir maximum adsorption capacity for Cl- onto CLDH and Na+ onto acid-treated zeolite was 116.3 and 28.4 mg/g, respectively. The Na+ uptake was greatly enhanced by solution pre-treatment (dechlorination) using CLDH, and also by zeolite acid treatment (with 1M = 2 M > 0.1 M > untreated, irrespective of acid type). Pre-conditioning the zeolite with Na+ prior to acid treatment also improved the adsorption capacity and promoted crystallinity. Desalination of potash brine-impacted groundwater was systematically investigated. Under the optimal conditions, the dual-adsorbent reduced the concentration of Cl- by 95.8%, Ca2+ by 89.8%, Mg2+ by 92.3%, Na+ by 91.9%, K+ by 96.5%, preserved a neutral pH (7.72), and lowered the sodium adsorption ratio (36.5 to 12.5) and the hardness (574 to 56.3 mg/L as CaCO3). In contrast, natural zeolite alone only removed 51.2% of the Na+ and 79.6% of the K+, and also generated extremely hard water (3620 mg/L as CaCO3) due to Ca2+ and Mg2+ exchange. Finally, zeolite regeneration studies were conducted using 0.1 M HCl. The Na+ was efficiently desorbed, but K+ remained. Over four consecutive adsorption–desorption cycles, the net K+ loading increased from 4.8 to 21.2 mg/g. This K-form zeolite could potentially be applied as a slow-release fertilizer, thereby transforming a potash mining waste material into a valuable resource.

Description

Keywords

Zeolite, Layered double hydroxide, Desalination, Sodium adsorption, Potassium adsorption, Chloride adsorption, Regeneration

Citation

Degree

Master of Science (M.Sc.)

Department

Civil and Geological Engineering

Program

Environmental Engineering

Citation

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DOI

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