01451nam a2200217Ia 4500 MX-MdCICY 20260521091204.0 CICY B-10170 Hydrogen Production from Simulated Hot Coke Oven Gas by Using Oxygen-Permeable Ceramics Energy & Fuels, 23(1), p.414-421, 2009 Hydrogen production from simulated hot coke oven gas (HCOG)was investigated in a BaCo0.7Fe0.2Nb0.1O3-ä (BCFNO)membrane reactor combined with a Ni/Mg(Al)O catalyst by the partial oxidation with toluene as a model tar compound under atmospheric pressure. The reaction results indicated that toluene was completely converted to H2 and CO in the catalytic reforming of the simulated HCOG in the temperature range from 825 to 875 °C. Both thermodynamically predicated values and experimental data showed that the selective oxidation of toluene took precedence over that of CH4 in the reforming reaction. At optimized reaction conditions, the dense oxygen-permeable membrane has an oxygen permeation flux around 12.3 mL cm-2 min-1, and a CH4 conversion of 86 Cheng, H. Zhang, Y. Lu, X. Ding, W. Li, Q. https://drive.google.com/file/d/1LkJXWg4zqi4jHIv5F27jeZaQ1IaUBcxf/view?usp=drivesdk Para ver el documento ingresa a Google con tu cuenta: @cicy.edu.mx Loc REF1 250602s9999 xx |||||s2 |||| ||und|d 20348 20348 0 0 Loc 0 0 F1 CICY CICY RE 2025-06-25 0 B-10170 2025-06-25 14:06:26 2025-06-25 REF1