<p>This paper highlights the recovery of high-quality materials from bauxite mining waste. Oxalic acid is used to remove iron oxides (Fe<sub>2</sub>O<sub>3</sub>) by leaching process. The leaching process for Fe<sub>2</sub>O<sub>3</sub> was thoroughly optimized by carefully controlling the oxalic acid concentration, temperature, and extraction time. The variables were systematically adjusted within the ranges of 0.5–2M for acid concentration, 50–80°C for temperature, and 30–240 minutes for extraction time. The optimized conditions for leaching with oxalic acid are 1.5 molar at 70°C and 210 min with removal of iron oxide was 65.18%. These conditions represent the pinnacle of efficiency, ensuring maximum Fe<sub>2</sub>O<sub>3</sub> removal from the waste material. The apparent activation energy is 18.36 KJmol<sup>-1</sup> and 35.38 KJmol<sup>-1</sup> for Chemical reaction model and Diffusion model for the Oxalic acid Leaching (shrinking core model). A robust statistical design, known as Box-Behnken, was rigorously implemented using Minitab to enhance and optimize the process. The product obtained from PLK rock is a highly valued material for filler industrial applications like textile, paper, rubber, ceramic, filler, paint, and refractory industries.</p>

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Statistical design and kinetic study on leaching behavior of Khondalite rocks for filler industrial applications

  • Rudra Narayan Mohapatro,
  • Ranjita Swain,
  • Sunita Routray,
  • Satyabrata Mohanta

摘要

This paper highlights the recovery of high-quality materials from bauxite mining waste. Oxalic acid is used to remove iron oxides (Fe2O3) by leaching process. The leaching process for Fe2O3 was thoroughly optimized by carefully controlling the oxalic acid concentration, temperature, and extraction time. The variables were systematically adjusted within the ranges of 0.5–2M for acid concentration, 50–80°C for temperature, and 30–240 minutes for extraction time. The optimized conditions for leaching with oxalic acid are 1.5 molar at 70°C and 210 min with removal of iron oxide was 65.18%. These conditions represent the pinnacle of efficiency, ensuring maximum Fe2O3 removal from the waste material. The apparent activation energy is 18.36 KJmol-1 and 35.38 KJmol-1 for Chemical reaction model and Diffusion model for the Oxalic acid Leaching (shrinking core model). A robust statistical design, known as Box-Behnken, was rigorously implemented using Minitab to enhance and optimize the process. The product obtained from PLK rock is a highly valued material for filler industrial applications like textile, paper, rubber, ceramic, filler, paint, and refractory industries.