Article ID Journal Published Year Pages File Type
42570 Applied Catalysis A: General 2009 6 Pages PDF
Abstract

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%.

Graphical abstractContinuous 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 full-size imageDownload as PowerPoint slide

Related Topics
Physical Sciences and Engineering Chemical Engineering Catalysis
Authors
, , ,