In this study, hydroxyapatite (HAp) is investigated as a catalyst support for Fischer–Tropsch synthesis (FTS) using iron as the active metal. The reaction is performed in a continuous stirred-tank reactor (CSTR), providing superior temperature control and enhanced gas–solid interactions. The Fe/HAp catalyst is benchmarked against a commercial ferric oxide catalyst (Nanocat®), and the effects of the CO/H2 feed ratio, temperature, and gas space velocity (SV) on the catalytic performance are evaluated. X-ray diffraction (XRD) analysis reveals strong Fe–HAp interactions, leading to iron phosphide (Fe2P) formation, which enhances iron dispersion and mitigates sintering. Scanning transmission electron microscopy with energy-dispersive X-ray spectroscopy (STEM-EDS) confirms a uniform iron distribution with an average particle size of 5 nm. Performance tests show that Fe/HAp maintains stable CO conversion (40 %) at a high SV (12,050 mL·g−1·h−1, 250 °C), whereas Nanocat® deactivates rapidly, mainly due to severe sintering. Both catalysts exhibit high C5+ hydrocarbon selectivity (>90 %); Fe/HAp favors gasoline (32 %), while Nanocat® favors diesel (33 %) at 250 °C. Notably, Fe/HAp promotes olefin selectivity (50 %) at 220 °C and an H2/CO ratio of 1, whereas increasing the H2/CO ratio to 2 enhances oxygenate formation (35 %). These findings highlight HAp as a promising support for modifying Fischer–Tropsch selectivity while ensuring catalyst stability.
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