کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
42570 | 45931 | 2009 | 6 صفحه PDF | دانلود رایگان |

The continuous lumping approach was used for modeling of hydrocracking of heavy crude oil at moderate reaction conditions. The model parameters were estimated from experimental results obtained in an isothermal fixed bed reactor at different temperatures (380–420 °C) and space velocity (1.5, 0.5 and 0.33 h−1) at constant pressure and hydrogen-to-oil ratio of 9.8 MPa and 5000 ft3/bbl respectively. Four model parameters showed linear trend with temperature whereas only one parameter remained almost constant. The optimized values of model parameters were employed to predict results obtained at different reaction conditions from which they were derived. Comparisons between experimental data and predictions using the continuous lumping kinetic model showed good agreement with average absolute error lower than 5%.
Continuous lumping approach was used for modeling heavy crude oil hydrocracking. Model parameters were estimated from experimental results obtained at different temperatures and space velocities at constant pressure and hydrogen-to-oil ratio. Four model parameters showed linear trend with temperature whereas one parameter remained almost constant. Optimized values of model parameters were employed to predict results obtained at different reaction conditions from which they were derived. Comparisons between experimental data and predictions using the continuous lumping kinetic model showed good agreement.Figure optionsDownload as PowerPoint slide
Journal: Applied Catalysis A: General - Volume 365, Issue 2, 31 August 2009, Pages 237–242