Fluid catalytic cracking modeling and simulation are based upon different kinetic modeling .The kinetic models are classified on the basis of chemical entities. The entities are ?lumps? based on boiling point , chemical type and structured oriented lumping . Boiling point based lump models are easy to simulate because they have less complexity and required least amount of data, where as chemical type and structured based modeling require detail analysis of feed and data to calibrate the kinetic parameters. Pseducomponents based modeling approach for the kinetic parameter estimation, eliminates the need for determining a large number of rate constant required in conventional lumped models. Kinetic model play a important role in effective sim...
YesFluid Catalytic Cracking (FCC) unit is an important unit of modern refineries and any improvement...
Keywords: fluid catalytic cracking, steady-state model, dynamic model The fluid catalytic cracking p...
In the present work, a one dimensional heterogeneous two phase model of the adiabatic FCC reactor as...
A one-dimensional mathematical modelling and simulation of the riser reactor in a fluid catalytic cr...
AbstractThe paper presents the research and the results obtained by the author concerning the kineti...
Computational fluid-dynamic (CFD) is a useful tool to understand the performance and help the desig...
YesIn this work a simulation of detailed steady state model of an industrial fluid catalytic crackin...
A 45 mL bench-scale internal recycle reactor, named a \u27Riser Simulator\u27 was used to study the ...
Fluidized Catalytic Cracking (FCC) is the primary conversion process in modern oil refining. It uses...
The catalytic cracking of hydrocarbons in a FCC riser is a very complex physical and chemical phenom...
Fluid catalytic cracking unit (FCCU) performs the most vital role in modern refinery process because...
In this study a comparison of 3-lump and 4-lump kinetic models predicting the yield of gas...
The riser reactor is a highly effective reactor for fast gas-solid reaction systems. In spite of ext...
Models which describe the performance of the riser and regenerator reactors of fluid catalytic crack...
ANSYS Fluent is used to examine the mixing of catalyst zeolite particles with petroleum feedstock an...
YesFluid Catalytic Cracking (FCC) unit is an important unit of modern refineries and any improvement...
Keywords: fluid catalytic cracking, steady-state model, dynamic model The fluid catalytic cracking p...
In the present work, a one dimensional heterogeneous two phase model of the adiabatic FCC reactor as...
A one-dimensional mathematical modelling and simulation of the riser reactor in a fluid catalytic cr...
AbstractThe paper presents the research and the results obtained by the author concerning the kineti...
Computational fluid-dynamic (CFD) is a useful tool to understand the performance and help the desig...
YesIn this work a simulation of detailed steady state model of an industrial fluid catalytic crackin...
A 45 mL bench-scale internal recycle reactor, named a \u27Riser Simulator\u27 was used to study the ...
Fluidized Catalytic Cracking (FCC) is the primary conversion process in modern oil refining. It uses...
The catalytic cracking of hydrocarbons in a FCC riser is a very complex physical and chemical phenom...
Fluid catalytic cracking unit (FCCU) performs the most vital role in modern refinery process because...
In this study a comparison of 3-lump and 4-lump kinetic models predicting the yield of gas...
The riser reactor is a highly effective reactor for fast gas-solid reaction systems. In spite of ext...
Models which describe the performance of the riser and regenerator reactors of fluid catalytic crack...
ANSYS Fluent is used to examine the mixing of catalyst zeolite particles with petroleum feedstock an...
YesFluid Catalytic Cracking (FCC) unit is an important unit of modern refineries and any improvement...
Keywords: fluid catalytic cracking, steady-state model, dynamic model The fluid catalytic cracking p...
In the present work, a one dimensional heterogeneous two phase model of the adiabatic FCC reactor as...