4.7 Article

The effects of (di-,tri-valent)-cation partitioning and intercalant anion-type on the solubility of hydrotalcites

Journal

JOURNAL OF THE AMERICAN CERAMIC SOCIETY
Volume 103, Issue 10, Pages 6025-6039

Publisher

WILEY
DOI: 10.1111/jace.17324

Keywords

hydrotalcite-like minerals; LDH; solubility constant; thermodynamics

Funding

  1. Consejo Nacional de Ciencia y Tecnologia
  2. Universidad Autonoma de Nuevo Leon
  3. UC-Mexus Program of the University of California
  4. U.S.-China Clean Energy Research Center on Water Energy Technologies
  5. Federal Highway Administration [DTFH61-13-H-00011]
  6. U.S. National Science Foundation [1066583, 1401533]
  7. Electric Power Research Institute
  8. Directorate For Engineering [1066583] Funding Source: National Science Foundation
  9. Div Of Civil, Mechanical, & Manufact Inn [1066583] Funding Source: National Science Foundation

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Synthetic hydrotalcites were produced by a co-precipitation method. The hydrotalcites are represented by the general formula [(M(1-x)M(x)III)-M-II(OH)(2)][A(n-)](x/n)center dot zH(2)O, where M(II)is a divalent cation (eg, Mg(2+)or Ca2+), M(III)is a trivalent cation (eg, Al3+) and A(n-)is the interlayer anion. Herein, M-II = Mg, and M-III = Al such that [Mg/Al] = [2, 3] (atomic units) and A(n-), represents intercalant species including: OH-, SO(4)(2-)and CO(3)(2-)anions. The thermochemical data of each compound including their solubility constants (K-so), density and molar volume were quantified at T = 25 +/- 0.5 degrees C, andP = 1 bar. The solubilities of the synthetic hydrotalcites, irrespective of their divalent-trivalent cation partitioning ratio, scaled as CO32- < SO42- < OH-; in order of decreasing solubility. The type of anion, very slightly, affected the solubility with less than +/- 1 log unit of variation for [Mg/Al] = 2, and +/- 2 log units of variation for [Mg/Al] = 3. The solubilities of these phases were strongly correlated with that of gibbsite (Al(OH)(3)); such that activity of the [AlO2-] species wassolubility determiningwith increasing pH. The tabulated thermodynamic data were used to construct solid-solution models for phases encompassing both cation distribution ratios and to calculate stable phase equilibria relevant to alkali-activated slag (AAS) systems for diverse activator compositions.

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