Summarization: A steady state model is formulated to describe the reactions between one gaseous and two non-volatile components on partially wetted catalysts in a trickle-bed reactor. Unlike previous studies, the model does not assume a gaseous or liquid limiting reactant. The computed results show the effect of intraparticle and interphase mass transfer resistances as well as of wetting efficiency and number and location of wetted zones on catalyst performance. Maximum effectiveness factors are generally obtained with intermediate values of the wetting efficiency. The model is applied to a typical HDS process of heavy gas oil in trickle-bed reactors.Presented on: Chemical Engineering Scienc
A pilot-scale countercurrent trickle bed reactor (TBR), packed with a water-repellent catalyst, is i...
An improved hydrodynamic model is developed for estimating wetting efficiency, pressure drop, and li...
AbstractLaboratory-scale trickle bed reactors are often used in testing of catalyst life time and ac...
Abstract-A steady state model is formulated to describe the reactions between one gaseous and two no...
Most trickle-bed reactors utilize cocurrent, downward flow of gas and liquid reactants through a fix...
A steady state model of a trickle bed reactor is developed for the consecutive hydrogenation of 1,5,...
A new development in the field of internals in packed columns is the use of structured packing types...
The purpose of this research is to provide fundamental insight into the partial wetting of catalyst ...
In trickle-bed reactors (TBRs), gas and liquid reactants flow co-currently downward through a packe...
The HDS, HDN, hydrodeoxygenation, hydrocracking, and saturative hydrogenation of middle distillates ...
Comprehensive CFD-model for reactive flow of gas and liquid in porous catalyst beds was developed an...
An experimental study was carried out to investigate whether the use of structured packings might im...
Successful transfer of multiphase catalytic reactions from laboratory to commercial scale depends on...
Stationary kinetic methods are not sufficient for studying chemical processes in which solid heterog...
An experimental study was carried out to investigate whether the use of structured packings might im...
A pilot-scale countercurrent trickle bed reactor (TBR), packed with a water-repellent catalyst, is i...
An improved hydrodynamic model is developed for estimating wetting efficiency, pressure drop, and li...
AbstractLaboratory-scale trickle bed reactors are often used in testing of catalyst life time and ac...
Abstract-A steady state model is formulated to describe the reactions between one gaseous and two no...
Most trickle-bed reactors utilize cocurrent, downward flow of gas and liquid reactants through a fix...
A steady state model of a trickle bed reactor is developed for the consecutive hydrogenation of 1,5,...
A new development in the field of internals in packed columns is the use of structured packing types...
The purpose of this research is to provide fundamental insight into the partial wetting of catalyst ...
In trickle-bed reactors (TBRs), gas and liquid reactants flow co-currently downward through a packe...
The HDS, HDN, hydrodeoxygenation, hydrocracking, and saturative hydrogenation of middle distillates ...
Comprehensive CFD-model for reactive flow of gas and liquid in porous catalyst beds was developed an...
An experimental study was carried out to investigate whether the use of structured packings might im...
Successful transfer of multiphase catalytic reactions from laboratory to commercial scale depends on...
Stationary kinetic methods are not sufficient for studying chemical processes in which solid heterog...
An experimental study was carried out to investigate whether the use of structured packings might im...
A pilot-scale countercurrent trickle bed reactor (TBR), packed with a water-repellent catalyst, is i...
An improved hydrodynamic model is developed for estimating wetting efficiency, pressure drop, and li...
AbstractLaboratory-scale trickle bed reactors are often used in testing of catalyst life time and ac...