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The outcomes showed that a more substantial solid-liquid proportion, an increased heat, and a reduced pH worth of the leaching option had been good for the release of Cr(III) and NH4+-N from the tannery sludge. The production kinetics of Cr(III) and NH4+-N used parabolic diffusion and easy Elovich designs both in the static and powerful leaching circumstances, showing that the production had been a complex heterogeneous diffusion process. The NH4+-N was simple to be leached aside as well a
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