A simplified catalyst deactivation model was proposed in this work to evaluate the catalyst life character. The model mainly considered the effect of coking deposition on the catalyst deactivation. A three-lumped kinetic model based on the catalyst deactivation model was established to describe the coal tar hydrogenation process, and model parameters were determined by means of fitting the experimental hydrogenation data. Validation results revealed that the model could predict the overall trend of catalyst deactivation effectively. This work serves as a significant guidance for the design and optimization of a hydrogenation catalyst
In catalytic processes with catalyst deactivation, there is a big problem in estimating the remainin...
Several aspects of catalyst deactivation have been studied with reference toselective acetylene hydr...
Changes in the quality of the feedstocks generated by involving various petroleum fractions in catal...
This paper presents the study of the kinetics of the primary destructive coal tar hydrogenation at c...
A new carbon-number-based kinetic model containing 18 hydrocarbon groups was developed in this work ...
Hydrogenation technology is an indispensable chemical upgrading process for converting the heavy fee...
A new eight-lump kinetic model containing 19 kinetic constants is proposed to describe coal tar hydr...
A new carbon-number-based kinetic model containing 18 hydrocarbon groups was developed in this work ...
A Spanish subbituminous coal was catalytically hydrogenated and catalyst deactivation was investigat...
In catalytic processes with catalyst deactivation, there is a big problem in estimating the remainin...
In catalytic processes with catalyst deactivation, there is a big problem in estimating the remainin...
The decay of catalyst activity in solid-catalyzed reactions is of great commercial importance, since...
The decay of catalyst activity in solid-catalyzed reactions is of great commercial importance, since...
This paper presents the study of the kinetics of the primary destructive coal tar hydrogenation at c...
This paper presents the study of the kinetics of the primary destructive coal tar hydrogenation at c...
In catalytic processes with catalyst deactivation, there is a big problem in estimating the remainin...
Several aspects of catalyst deactivation have been studied with reference toselective acetylene hydr...
Changes in the quality of the feedstocks generated by involving various petroleum fractions in catal...
This paper presents the study of the kinetics of the primary destructive coal tar hydrogenation at c...
A new carbon-number-based kinetic model containing 18 hydrocarbon groups was developed in this work ...
Hydrogenation technology is an indispensable chemical upgrading process for converting the heavy fee...
A new eight-lump kinetic model containing 19 kinetic constants is proposed to describe coal tar hydr...
A new carbon-number-based kinetic model containing 18 hydrocarbon groups was developed in this work ...
A Spanish subbituminous coal was catalytically hydrogenated and catalyst deactivation was investigat...
In catalytic processes with catalyst deactivation, there is a big problem in estimating the remainin...
In catalytic processes with catalyst deactivation, there is a big problem in estimating the remainin...
The decay of catalyst activity in solid-catalyzed reactions is of great commercial importance, since...
The decay of catalyst activity in solid-catalyzed reactions is of great commercial importance, since...
This paper presents the study of the kinetics of the primary destructive coal tar hydrogenation at c...
This paper presents the study of the kinetics of the primary destructive coal tar hydrogenation at c...
In catalytic processes with catalyst deactivation, there is a big problem in estimating the remainin...
Several aspects of catalyst deactivation have been studied with reference toselective acetylene hydr...
Changes in the quality of the feedstocks generated by involving various petroleum fractions in catal...