The goal of this study was to evaluate hydrodynamic influence on experimental HDS catalyst activity measurement carried out in pilot scale trickle-bed reactor. Hydrodynamic data were evaluated by RTD method in laboratory glass model of pilot reactor. Mathematical models of the process were formulated both like 1D pseudohomogeneou and 3D heterogeneous ones. The aim of this work was to forecast interaction between intrinsic reaction kinetic, hydrodynamics and mass transfer
An adiabatic trickle bed reactor was developed and simulated numerically to study the dynamic behavi...
Summarization: A steady state model is formulated to describe the reactions between one gaseous and ...
AbstractExperimental evaluation and dynamic modelling were presented for the transient behavior of a...
AbstractLaboratory-scale trickle bed reactors are often used in testing of catalyst life time and ac...
Trickle bed reactors (TBRs) are commonly used in chemical industries. Scale-up of TBR is difficult a...
In trickle-bed reactors (TBRs), gas and liquid reactants flow co-currently downward through a packe...
The study was fosussed on identification of flow parameters of gas and liquid phases during hydrodes...
In this paper, the influence of the hydrodynamic effects on the plug flow model deviation in the hyd...
The HDS, HDN, hydrodeoxygenation, hydrocracking, and saturative hydrogenation of middle distillates ...
Commercial HDT processes usually operate in a trickle-bed regime, with co-current downward flow of g...
The hydrodesulfurization (HDS), hydrodenitrogenation (HDN), hydrodeoxygenation, hydrocraking and sat...
The impacts of the packing characteristics on the hydrodynamics od a trickle bed reactor (TBR) have ...
Comprehensive CFD-model for reactive flow of gas and liquid in porous catalyst beds was developed an...
An Euler-Euler computational fluid model was developed successfully for the hydrodynamic prediction ...
Hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) of middle distillates over a commercial Ni...
An adiabatic trickle bed reactor was developed and simulated numerically to study the dynamic behavi...
Summarization: A steady state model is formulated to describe the reactions between one gaseous and ...
AbstractExperimental evaluation and dynamic modelling were presented for the transient behavior of a...
AbstractLaboratory-scale trickle bed reactors are often used in testing of catalyst life time and ac...
Trickle bed reactors (TBRs) are commonly used in chemical industries. Scale-up of TBR is difficult a...
In trickle-bed reactors (TBRs), gas and liquid reactants flow co-currently downward through a packe...
The study was fosussed on identification of flow parameters of gas and liquid phases during hydrodes...
In this paper, the influence of the hydrodynamic effects on the plug flow model deviation in the hyd...
The HDS, HDN, hydrodeoxygenation, hydrocracking, and saturative hydrogenation of middle distillates ...
Commercial HDT processes usually operate in a trickle-bed regime, with co-current downward flow of g...
The hydrodesulfurization (HDS), hydrodenitrogenation (HDN), hydrodeoxygenation, hydrocraking and sat...
The impacts of the packing characteristics on the hydrodynamics od a trickle bed reactor (TBR) have ...
Comprehensive CFD-model for reactive flow of gas and liquid in porous catalyst beds was developed an...
An Euler-Euler computational fluid model was developed successfully for the hydrodynamic prediction ...
Hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) of middle distillates over a commercial Ni...
An adiabatic trickle bed reactor was developed and simulated numerically to study the dynamic behavi...
Summarization: A steady state model is formulated to describe the reactions between one gaseous and ...
AbstractExperimental evaluation and dynamic modelling were presented for the transient behavior of a...