Leaching Kinetics and Reactive Regulation of Boiling Furnace Pyrite Cinder (BPC) in an Oxalic Acid-Sulfuric Acid System

To address the challenge of low iron extraction efficiency from boiling furnace pyrite cinder (BPC), a significant secondary iron resource posing environmental risks due to massive stockpiling in China, this study investigated the kinetics and reactivity regulation of an oxalic acid-sulfuric acid hybrid leaching system to overcome the inertness and diffusion barriers of hematite. Single-factor experiments and Response Surface Methodology (RSM) optimization were employed to determine optimal leaching parameters (time, temperature, liquid–solid ratio, H2SO4 concentration) under constant stirring (400 r/min) and BPC–oxalic acid ratio (50:1). Shrinking core kinetic modeling, complemented by SEM-EDS/XRD residue characterization, elucidated the dissolution mechanism. Results showed a maximum iron leaching rate of 94.7% at 90 °C, 40 wt% H2SO4, an L/S ratio of 5 mL/g, and a time of 7 h. Kinetics transitioned from liquid-film diffusion control (Ea = 76.9 kJ/mol) below 70 °C to mixed interfacial reaction/internal diffusion control (Ea = 32.4 kJ/mol) above 80 °C. Highly concentrated acid conditions (50% H2SO4) reduced efficiency by >20% due to oxalate protonation, CaSO4 pore occlusion, and increased viscosity. RSM confirmed temperature-dominated kinetics and acid concentration-governed thermodynamics, with no synergy under combined high-temperature/high-acidity conditions. This optimized process enables efficient iron recovery from refractory BPC using minimal reagent consumption.