In this work was done a fluid dynamic study in an experimental packed reactor using RTD exposing bimodal and modal behavior when it was varied the particle diameter and bed presenting flow channels, dead zones in the vessel and lateness of the material mixture in the equipment. Additionally, using flow pattern models was estimated the chemical conversion with greater approximation to the experimental value. This result could be use in the scaling stages of the process and minimize overdesigns
Chlorination of hydrocarbons is an industrially important process used for the production of commerc...
Stirred tank reactors are widely used in process industries due to their flexible mode of operation....
A radiotracer study was carried out in a trickle bed reactor (TBR) independently filled with two dif...
Packed bed reactors are used in many chemical processes. With the advent of modern computers, flow s...
Packed bed reactors are used in many chemical processes. With the advent of modern computers, flow s...
AbstractMean Residence Time (MRT) was determined numerically for the pilot packed bed reactor filled...
International audienceThe Residence-Time Distribution (RTD) is a chemical engineering concept introd...
The Residence-Time Distribution (RTD) is a chemical engineering concept introduced by Danckwerts in ...
The continuous operation of a stirred tank reactor for styrene polymerization was modeled. The propo...
Trickle bed reactors (TBR), as typical packed bed reactors (PBR), are widely used in various fields....
In many cases, quick methods are needed to evaluate the conversion and yield that may occur in a giv...
Themain objective of this projectis to investigate the hydrodynamic characteristics of co-current u...
The main objective ofthis project is to investigate the hydrodynamic characteristics of co-current ...
The main objective ofthis project is to investigate the hydrodynamic characteristics of co-current ...
The residence time distribution (RTD) of a pilot plant scale packed bed reactor was studied in the ...
Chlorination of hydrocarbons is an industrially important process used for the production of commerc...
Stirred tank reactors are widely used in process industries due to their flexible mode of operation....
A radiotracer study was carried out in a trickle bed reactor (TBR) independently filled with two dif...
Packed bed reactors are used in many chemical processes. With the advent of modern computers, flow s...
Packed bed reactors are used in many chemical processes. With the advent of modern computers, flow s...
AbstractMean Residence Time (MRT) was determined numerically for the pilot packed bed reactor filled...
International audienceThe Residence-Time Distribution (RTD) is a chemical engineering concept introd...
The Residence-Time Distribution (RTD) is a chemical engineering concept introduced by Danckwerts in ...
The continuous operation of a stirred tank reactor for styrene polymerization was modeled. The propo...
Trickle bed reactors (TBR), as typical packed bed reactors (PBR), are widely used in various fields....
In many cases, quick methods are needed to evaluate the conversion and yield that may occur in a giv...
Themain objective of this projectis to investigate the hydrodynamic characteristics of co-current u...
The main objective ofthis project is to investigate the hydrodynamic characteristics of co-current ...
The main objective ofthis project is to investigate the hydrodynamic characteristics of co-current ...
The residence time distribution (RTD) of a pilot plant scale packed bed reactor was studied in the ...
Chlorination of hydrocarbons is an industrially important process used for the production of commerc...
Stirred tank reactors are widely used in process industries due to their flexible mode of operation....
A radiotracer study was carried out in a trickle bed reactor (TBR) independently filled with two dif...